US10851392B2 - Method for producing methacrylic acid ester - Google Patents

Method for producing methacrylic acid ester Download PDF

Info

Publication number
US10851392B2
US10851392B2 US14/405,593 US201314405593A US10851392B2 US 10851392 B2 US10851392 B2 US 10851392B2 US 201314405593 A US201314405593 A US 201314405593A US 10851392 B2 US10851392 B2 US 10851392B2
Authority
US
United States
Prior art keywords
particularly preferable
methacrylic acid
acid ester
alcohol
coa
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
US14/405,593
Other versions
US20150184207A1 (en
Inventor
Eiji Sato
Fujio Yu
Wataru Mizunashi
Eiji Nakajima
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Chemical Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=50236843&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=US10851392(B2) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Mitsubishi Chemical Corp filed Critical Mitsubishi Chemical Corp
Assigned to MITSUBISHI RAYON CO., LTD. reassignment MITSUBISHI RAYON CO., LTD. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: NAKAJIMA, EIJI, MIZUNASHI, WATARU, YU, FUJIO, SATO, EIJI
Publication of US20150184207A1 publication Critical patent/US20150184207A1/en
Assigned to MITSUBISHI CHEMICAL CORPORATION reassignment MITSUBISHI CHEMICAL CORPORATION CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). Assignors: MITSUBISHI RAYON CO., LTD.
Application granted granted Critical
Publication of US10851392B2 publication Critical patent/US10851392B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00—Preparation of oxygen-containing organic compounds
    • C12P7/62—Carboxylic acid esters
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/20—Bacteria; Culture media therefor
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N15/00—Mutation or genetic engineering; DNA or RNA concerning genetic engineering, vectors, e.g. plasmids, or their isolation, preparation or purification; Use of hosts therefor
    • C12N15/09—Recombinant DNA-technology
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/10—Transferases (2.)
    • C12N9/1025—Acyltransferases (2.3)
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12Y—ENZYMES
    • C12Y203/00—Acyltransferases (2.3)
    • C12Y203/01—Acyltransferases (2.3) transferring groups other than amino-acyl groups (2.3.1)
    • C12Y203/01084—Alcohol O-acetyltransferase (2.3.1.84)

Definitions

  • the present invention relates to a method for producing methacrylic acid ester using a biocatalyst.
  • Methacrylic acid esters are primarily used as raw material in acrylic resins, and there are many demands also as a monomer in fields such as paints, adhesives, and resin modifiers.
  • ACH acetone cyano hydrin
  • Patent Document 5 exemplifies various biocatalysts (hydrolase, wax ester synthetase, alcohol acetyltransferase) having general ester formation activity; however, it is unclear whether the exemplified biocatalysts have synthetic activity for methacrylic acid ester.
  • Patent Document 6 discloses a method for producing acrylic acid ester by causing hydrolase to function under the presence of acrylyl-CoA and alcohol.
  • the same document suggests that production is similarly possible also for methacrylic acid esters.
  • it merely illustrates that the production of a part of acrylic acid esters is possible with hydrolase, and it is unclear whether methacrylic acid esters having a different structure are similarly producible by hydrolase.
  • it is completely unclear whether it is possible to produce with other types of biocatalysts having different reaction mechanisms.
  • synthesizing esters by the hydrolase described in Patent Document 6 it is assumed that the formed ester will be decomposed by the hydrolysis activity in the first place, and thus is quite unlikely as an effective production method.
  • Patent Document 7 proposes synthesis methods of various esters that are fruit flavors. However, it has not been reported whether methacrylic acid esters are synthesizable with these enzymes, and has been completely unclear.
  • the present invention has an object of providing a method for producing methacrylic acid ester by way of a biocatalyst.
  • alcohol acyltransferase has activity for synthesizing methacrylic acid esters, thereby arriving at completion of the present invention. More specifically, the present invention is as follows.
  • a method for producing methacrylic acid ester includes a step of synthesizing methacrylic acid ester by causing an alcohol or phenol to act on methacrylyl-CoA under the presence of an alcohol acyltransferase.
  • the methacrylic acid ester is accumulated in at least 0.001 mM.
  • the method for producing methacrylic acid ester as described in the first or second aspect further includes a step of producing methacrylyl-CoA from isobutyryl-CoA or 3-hydroxyisobutyryl-CoA.
  • the isobutyryl-CoA is produced from 2-oxoisovaleric acid.
  • the alcohol acyltransferase is of plant origin.
  • the plant belongs to any order selected from the group consisting of Zingiberales, Rosales, Ericales, Cucurbitales, Brassicales and Laurales.
  • the plant belongs to any family selected from the group consisting of Musaceae, Rosaceae, Ericaceae, Actinidiaceae, Cucurbitaceae, Caricaceae and Lauraceae.
  • the plant belongs to any genus selected from the group consisting of Musa, Fragaria, Malus, Prunus, Pyrus, Vaccinium, Actinidia, Cucumis, Carica and Persea.
  • the plant in the method for producing methacrylic acid ester as described in the fifth aspect, is any genus selected from Musa, Malus, Prunus, Pyrus, Vaccinium, Actinidia, Cucumis, Carica and Persea.
  • the plant in the method for producing methacrylic acid ester as described in the fifth aspect, is any genus selected from Musa, Malus, Pyrus, Actinidia, Cucumis, Carica and Persea.
  • the plant in the method for producing methacrylic acid ester as described in the fifth aspect, is any one selected from the group consisting of banana, strawberry, apple, Prunus mume, Pyrus communis , blueberry, kiwi, melon, papaya and avocado.
  • the plant in the method for producing methacrylic acid ester as described in the fifth aspect, is any one selected from the group consisting of banana, apple, Prunus mume, Pyrus communis , blueberry, kiwi, melon, papaya and avocado.
  • the plant in the method for producing methacrylic acid ester as described in the fifth aspect, is any one selected from the group consisting of banana, apple, Pyrus communis , kiwi, melon, papaya and avocado.
  • the method for producing methacrylic acid ester as described in any of the first to thirteenth aspects uses a genetically modified microorganism that has been gene transferred so as to express alcohol acyltransferase.
  • the present invention is as follows in another aspect.
  • a method for producing methacrylic acid ester produces the methacrylic acid ester using a microorganism belonging to Rhodococcus genus.
  • the method for producing methacrylic acid ester as described in the fifteenth aspect uses a microorganism belonging to the Rhodococcus genus having 16SrDNA that includes a nucleotide sequence having at least 95% identity to the nucleotide sequence of 16SrDNA shown in SEQ ID NO. 31.
  • the microorganism belonging to Rhodococcus genus is Rhodococcus erythropolis.
  • the method for producing methacrylic acid ester as described in the fifteenth or sixteenth aspect uses a derivative strain of the microorganism as the microorganism belonging to Rhodococcus genus.
  • the microorganism belonging to Rhodococcus genus is Rhodococcus erythropolis PR-4 strain or a derivative strain thereof.
  • the derivative strain is a genetically modified strain having a modification of at least one of (a) or (b) shown below.
  • the derivative strain in the method for producing methacrylic acid ester as described in the nineteenth or twentieth aspect, has a plasmid for alcohol acyltransferase and/or acyl-CoA dehydrogenase expression.
  • the production of methacrylic acid ester by way of a biocatalyst becomes possible.
  • fermentative production of methacrylic acid ester can also be achieved.
  • the energy, resources and load on the environment can be remarkably reduced compared to a conventional chemical production process, and it becomes possible to efficiently produce methacrylic acid ester.
  • FIG. 1 is a view showing the production steps from 3-hydroxyisobutyryl-CoA to methacrylic acid ester;
  • FIG. 2 is a view showing the production steps from 2-oxoisovaleric acid to methacrylic acid ester;
  • FIG. 3 is a view showing the structure of a plasmid for LigD homolog gene deletion
  • FIG. 4 is a view illustrating a preparation method for plasmid for gene deletion using the In Fusion method.
  • FIG. 5 is a view showing the structures of plasmids for ACD-AAT co-expression.
  • methacrylic acid ester is a compound expressed by Formula 1.
  • R represents a linear or branched C1-20 hydrocarbon group.
  • the hydrocarbon group may be of saturated or unsaturated non-cyclic type, or may be of saturated or unsaturated cyclic type. It is preferably a linear or branched C1-10 unsubstituted alkyl group, aralkyl group or aryl group.
  • a C1-8 alkyl group such as a methyl group, ethyl group, n-propyl group, isopropyl group, n-butyl group, isobutyl group, sec-butyl group, tert-butyl group, n-pentyl group, isopentyl group, tert-pentyl group, n-hexyl group, isohexyl group, 2-hexyl group, dimethylbutyl group, ethylbutyl group, heptyl group, octyl group, 2-ethylhexyl group; a benzyl group or a phenyl group.
  • Metal acid indicates a compound having the formula below, and also includes any salts or ionized forms thereof.
  • salts of methacrylic acid for example, sodium salts, potassium salts, calcium salts, magnesium salts, etc. can be exemplified.
  • methacrylyl-CoA is a compound expressed by the structural formula below.
  • Methacrylyl-CoA is known as a metabolic intermediate of valine within organisms.
  • the methacrylyl-CoA used in the present invention can be that produced by a known or novel method.
  • the synthesis method thereof the method of organochemically synthesizing coenzyme A with methacrylic anhydride (Methods in Enzymology, 324, 73-79 (2000)) or a synthesis method using an enzyme reaction are known.
  • methacrylyl-CoA transformed by the action of acyl-CoA dehydrogenase (EC 1.3.99.3) (hereinafter referred to as ACD) with isobutyryl-CoA as a raw material or methacrylyl-CoA (refer to FIG. 1 ) transformed by action of enoyl-CoA hydratase (EC 4.2.1.17) (hereinafter referred to as ECH) from 3-hydroxyisobutyryl-CoA can be favorably used.
  • the method of the present invention preferably further includes a step of producing methacrylyl-CoA from isobutyryl-CoA or 3-hydroxyisobutyryl-CoA.
  • the isobutyryl-CoA used in the present invention one produced from 2-oxoisovaleric acid can be used (refer to FIG. 2 ).
  • the method of the present invention may further include a step of producing isobutyryl-CoA from 2-oxoisovaleric acid.
  • the alcohols or phenols serving as raw materials in the production of the methacrylic acid ester in the present invention are compounds expressed by formula 2 below.
  • the structure of the alcohol or phenols corresponds to methacrylic acid ester; therefore, the structure thereof is defined the same as R in Formula 1, and represents a linear or branched C1-20 hydrocarbon group.
  • the hydrocarbon group may be of saturated or unsaturated non-cyclic type, or may be of saturated or unsaturated cyclic type.
  • the alcohol acyltransferase of the present invention (hereinafter referred to as AAT) is an enzyme having a catalytic action for synthesizing ester by causing the acyl group of acyl-CoA to transfer to the alcohol or phenol.
  • AAT is considered to participate in the formation of esters in various fruits.
  • AAT is known to be present in plants such as Zingiberales (banana), Rosales (strawberry, apple, pear, peach), Cucurbitales (melon), Ericales (kiwi), Lamiales (olive), Solanales (tomato), and Sapindales (lemon, mango).
  • the AAT used in the present invention is not particularly limited so long as being a catalyst of biological origin having a capacity to produce methacrylic acid ester with methacrylyl-CoA and alcohol or phenol as raw materials, and the kind and origin thereof are not of concern.
  • One of plant origin is preferable as the enzyme source, and thereamong, one categorized as an angiosperm is preferable.
  • the AAT suited to the present invention can be easily selected from the plants by the following method.
  • An appropriate part of the tissue is acquired by cutting as necessary.
  • a solution containing methacrylyl-CoA and an alcohol or phenol represented by Formula 2 are added to this cut part, shaken, and allowed to react for a certain time.
  • It is possible to confirm the synthetic activity by confirming the presence of methacrylic acid ester in this reaction solution by GC (gas chromatography). More specifically, for example, the sarcocarp or pericarp is cut, a solution containing 1 to 10 mM methacrylyl-CoA, 0.35 KCl and 5 to 50 times molar quantity of n-butanol is added thereto, and shaken for 1 to 10 hours at 30° C.
  • an AAT applicable to the present invention can be selected by confirming the presence of methacrylic acid ester by way of GC.
  • the enzyme source of AAT suited to the present invention is one belonging to any order selected from the group consisting of Zingiberales, Rosales, Ericales, Cucurbitales, Brassicales, Laurales, Poales, Arecales, Asparagales, Saxifragales, Caryophyllales, Vitales, Malpighiales, Oxalidales, Fabales, Sapindales, Malvales, Myrtales, Ranunculales, Solanales, Lamiales, Gentianales and Asterales. Thereamong, it is preferably one belonging to any order selected from the group consisting of Zingiberales, Rosales, Ericales, Cucurbitales, Brassicales and Laurales.
  • Plants of Musaceae and Zingiberaceaeare are preferable as those belonging to the order Zingiberales; plants of Rosaceae and Moraceae are preferable as those belonging to the order Rosales; plants of Ericaceae, Actinidiaceae, Ebenaceae and Theaceae are preferable as those belonging to the order Ericales; plants of Cucurbitaceae are preferable as those belonging to the order Cucurbitales; plants of Caricaceae and Brassicaceae are preferable as those belonging to the order Brassicales; plants of Lauraceae are preferable as those belonging to the order Laurales; plants of Bromeliaceae and Poaceae are preferable as those belonging to the order Poales; plants of Arecaceae are preferable as those belonging to the order Arecales; plants of Orchidaceae and Iridaceae are preferable as those belonging to the order Asparagales; plants of Grossulariaceae are preferable as those belonging to the order Saxifragales; plants of Caryophyllacea
  • a related species of the above-mentioned plants can also be employed. Thereamong, it is more preferably a plant belonging to Musacea, Rosaceae, Ericeae, Actinidiaceae, Cucurbitaceae, Caricaceae or Lauraceae.
  • plants of Musa are preferable as those belonging to the family Musaceae; plants of Zingiber are preferable as those belonging to the family Zingiberaceae; plants of Fragaria, Malus, Prunus, Pyrus, Eriobotrya, Chaenomeles, Rubus and Rosa are preferable as those belonging to the family Rosaceae; plants of Ficus are preferable as those belonging to the family Moraceae; plants of Vaccinium are preferable as those belonging to the family Ericaceae; plants of Actinidia are preferable as those belonging to the family Actinidiaceae; plants of Diospyros are preferable as those belonging to the family Ebenaceae; plants of Camellia are preferable as those belonging to the family Theaceae; plants of Cucumis and Citrullus are preferable as those belonging to the family Cucurbitaceae; plants of Carica and Vasconcellea are preferable as those belonging to the family Caricaceae; plants of Arabidopsis are preferable as those belonging to the family
  • plants belonging to Musa, Fragaria, Malus, PRunus, Pyrus, Vaccinium, Actinidia, Cucumis, Carica or Persea are more preferable. Furthermore, thereamong, plants belonging to Musa, Malus, Pyrus, Actinidia, Cucumis, Carica or Persea are particularly preferable.
  • banana, strawberry, apple, Japanese apricot, European pear, blueberry, kiwi, melon, papaya or avocado is more preferable. Furthermore, thereamong, banana, apple, European pear, kiwi, melon, papaya or avocado is particularly preferable.
  • the classifications of plant are defined following Botanical Journal of the Linnean Society, 2009, 161, 105121.
  • mode of use upon supplying AAT for reaction, mode of use is not particularly limited so long as exhibiting the above-mentioned catalytic activity, and it is possible to use the biological tissue or processed product thereof as is.
  • biological tissue the entire planta, plant organs (e.g., fruit, leaves, petals, stem, seed, etc.), or plant tissue (e.g., fruit skin, sarcocarp, etc.) can be used.
  • plant organs e.g., fruit, leaves, petals, stem, seed, etc.
  • plant tissue e.g., fruit skin, sarcocarp, etc.
  • the processed product thereof the crude enzyme liquid from extracting AAT from these biological tissues, purified enzyme, or the like can be exemplified.
  • the gene for the AAT is isolated, for example, introduced to a general host vector system, and the microorganism transformed by this vector system can be used.
  • the host as for bacteria, E. coli, Rhodococcus, Pseudomonas, Corynebacterium, Bacillus, Streptococcus, Streptomyces , etc. can be exemplified; as for yeast, Saccharomyces, Candida, Shizosaccharomyces and Pichia ; and as for filamentous fungus, Aspergillus , etc. can be exemplified. Among these, it is particularly easy to use bacteria, and is also preferable in efficiency.
  • AAT genes have been published (for example, refer to Patent Document 7).
  • a DNA probe is prepared based on this publication, and for example, a primer used in PCR is prepared, and this gene can be isolated by performing PCR.
  • AAT can be purified, and genetic information can be obtained by a genetic engineering method on the basis of proteins thereof.
  • AAT gene in the present invention it is not particularly limited so long as the translated product thereof has a capability of producing methacrylic acid ester, and is appropriately selected from among the AAT enzymes sources.
  • AAT apple-derived AAT gene SEQ ID NO: 2
  • strawberry-derived AAT gene SEQ ID NO: 4
  • strawberry-derived AAT gene SEQ ID NO: 6
  • genes coding proteins having activity to produce methacrylic acid ester from methacrylyl-CoA and alcohol including an amino acid sequence in which one or a plurality of amino acids have been substituted, deleted or added to a wild-type amino acid sequence are also included in the AAT genes of the present invention.
  • the term “plurality” refers to 1 to 40, preferably 1 to 20, and more preferably no more than 10.
  • a kit for mutation introduction using a site-directed mutagenesis method, for example, QuikChangeTM Site-Directed Mutagenesis Kit (Stratagene), GeneTailorTM Site-Directed Mutagenesis System (Invitrogen), TaKaRa Site-Directed Mutagenesis System (Mutan-K, Mutan-Super Express Km, etc.: Takara Bio), etc., by a known method such as the Kunkel method or Gapped duplex method.
  • the entire gene having a sequence including mutation may be artificially synthesized.
  • confirmation of the nucleotide sequence of DNA can be performed by sequence determination by a common method. For example, based on Sanger's method, it is possible to confirm the sequence using an appropriate DNA sequencer.
  • genes coding proteins having activity to produce methacrylic acid ester from methacrylyl-CoA and alcohol expressing at least 90% identity with the protein consisting of the wild-type amino acid sequence, preferably 95%, more preferably 99.5%, and even more preferably 99.9%, are also included.
  • genes hybridizing under stringent conditions to a polynucleotide having the complementary nucleotide sequence to the wild-type nucleotide sequence, and coding protein having activity to produce methacrylic acid ester from methacrylyl-CoA and alcohol are also included.
  • stringent conditions for example, it is possible to exemplify conditions of perform hybridization by maintaining a nylon membrane fixing the DNA at the same temperature while probing at 65° C.
  • drying conditions after hybridization for example, “2 ⁇ SSC, 0.1% SDS, 42° C.” and “1 ⁇ SSC, 0.1% SDS, 37° C.”, and as more stringent conditions, for example, conditions such as “1 ⁇ SSC, 0.1% SDS, 65° C.” and “0.5 ⁇ SSC, 0.1% SDS, 50° C.” can be exemplified.
  • genes coding protein having activity to produce methacrylic acid ester from methacrylyl-CoA and alcohol consisting of a nucleotide sequence having identity of at least 80%, more preferably at least 90%, and more preferably at least 95% are also included.
  • the codons of the above-mentioned AAT genes may be changed according to the codon frequency of use in the microorganism host used in genetic transformation.
  • identity of the sequence, when the case of a nucleotide sequence, is arrived at by aligning both nucleotide sequences so that the bases of the two nucleotide sequences to be compared match as much as possible, and then expressing a value arrived at by subtracting the number of matching bases from the total number of bases as a percentage.
  • appropriate gaps are inserted into one or both of the two sequences compared as necessary.
  • Such an alignment of sequences can be performed using a known program such as BLAST, FASTA, and CLUSTAL, for example.
  • the above-mentioned total number of bases becomes the number of bases arrived at by counting one gap as one base.
  • the identity is calculated by subtracting the matching number of bases from the total number of bases in the longer sequence. This similarly applies also for the identity of amino acid sequences.
  • the broth obtained by culturing these recombinant microorganisms as is, or use the bacterial cell obtained by a harvesting operation such as centrifugation from this broth, a processed product thereof, or the like.
  • a bacterial cell processed product a bacterial cell treated with acetone, toluene or the like, freeze-dried bacterial cells, disrupted bacterial cells, or noncellular extract from disrupted bacterial cells, crude enzyme extracted from these enzymes or purified enzyme, etc. can be exemplified.
  • Methacrylic acid ester can also be synthesized with isobutyryl-CoA or 3-hydroxyisobutyryl-CoA as a raw material by simultaneously introducing ACD gene or ECH gene with AAT gene (refer to FIG. 1 and FIG. 2 ). Furthermore, by combining and introducing 2-oxoisovaleric acid dehydrogenase gene (hereinafter referred to as BCKAD), it is also possible to synthesize methacrylic acid from 2-oxoisovaleric acid.
  • BCKAD 2-oxoisovaleric acid dehydrogenase gene
  • Magnetospirillum magneticum is particularly preferable as the microorganism classified as Magnetospirillum; Rhodospirillum rubrum, Rhodospirillum centenum and Rhodospirillum photometricum are particularly preferable as the microorganism classified as Rhodospirillum; Azospirillum lipoferum and Azospirillum brasilense are particularly preferable as the microorganism classified as Azospirillum; Tistrella mobilis is particularly preferable as the microorganism classified as Tistrella; Acidiphilium cryptum and Acidiphilium multivorum are particularly preferable as the microorganism classified as Acidiphilium; Rhodobacter sphaeroides and Rhodobacter capsulatus are particularly preferable as the microorganism classified as Rhodobacter; Paracoccus denitrificans and Paracoccus aminophilus are particularly preferable as the microorganism classified as Paracoccus; Ruegeria
  • microorganisms exemplified herein are obtainable from the American Type Culture Collection (ATCC), National Institute of Technology and Evaluation, Biotechnology Division, Biological Resource Center (NBRC), National Institute of Advanced Industrial Science and Technology, Patent Organism Depository (FERM), or the like.
  • ATCC American Type Culture Collection
  • NBRC National Institute of Technology and Evaluation
  • NBRC Biotechnology Division
  • FEM Patent Organism Depository
  • methacrylic acid ester can be performed by the following method.
  • a solution was prepared by adding alcohol or phenol represented by Formula 2 and methacrylyl-CoA to a solvent, and then allowing to dissolve or suspend. Then, AAT is brought into contact with this solution or suspension, and methacrylyl-CoA and the alcohol or phenol is allowed to react while controlling conditions such as temperature. By way of the reaction, a methacrylic group of methacrylyl-CoA is transferred to the alcohol or phenol of Formula 2, thereby causing methacrylic acid ester to be formed.
  • the solution containing the methacrylyl-CoA and alcohol or phenol represented by Formula 2 is normally prepared in an aqueous medium such as a buffer solution.
  • an osmotic pressure regulator it is sufficient if a water-soluble substance added with the object of adjusting the osmotic pressure of the solution such as the inside of the cell so as to make isotonic or hypertonic, and for example, is a salt or saccharide, and preferably a salt.
  • the salt is preferably a metallic salt, more preferably an alkali metal salt, even more preferably an alkali metal halide, and for example, sodium chloride and potassium chloride can be exemplified.
  • the saccharide is preferably a monosaccharide or oligosaccharide, more preferably a monosaccharide or disaccharide, and for example, glucose, sucrose, mannitol and the like can be exemplified.
  • the osmotic pressure regulator is preferably added at a concentration of at least 1 mM, and it is particularly preferable to regulate so as to make isotonic or hypertonic compared to a solution inside the biological cell used.
  • an organic solvent can be added in advance to make react in a two-phase system.
  • the organic solvent for example, a linear, branched or cyclic, saturated or unsaturated aliphatic hydrocarbon, saturated or unsaturated aromatic hydrocarbon, or the like can be used individually or by mixing two or more types.
  • hydrocarbon solvents e.g., pentane, hexane, cyclohexane, benzene, toluene, xylene, etc.
  • halogenated hydrocarbon solvents e.g., methylene chloride, chloroform, etc.
  • ether solvents e.g., diethyl ether, dipropyl ether, dibutyl ether, tert-butylmethyl ether, dimethoxyethane, etc.
  • ester solvents e.g., methyl formate, methyl acetate, ethyl acetate, butyl acetate, methyl propionate
  • the methacrylic acid ester formed will migrate to the organic phase, and the reaction may progress efficiently.
  • the molar ratios and concentrations of methacrylyl-CoA and the alcohol or phenol represented by Formula 2 in the reaction solution are arbitrary, and not particularly limited.
  • the amount of AAT used or reaction conditions are determined as appropriate according to the raw materials used.
  • the concentration of each raw material is set to the range of 0.0000001 to 10% by mass in the case of methacrylyl-CoA, and the alcohol or phenol is added at a concentration of 0.1 to 1000 times by moles, preferably 0.5 to 50 times by moles, relative to the methacrylyl-CoA used.
  • reaction temperature or reaction time are determined as appropriate according to the raw materials used, activity of enzyme, etc., and are not particularly limited; however, it is sufficient normally if allowed to react at 5 to 80° C. for 1 hour to 1 week. At 10 to 70° C., it is preferably for 1 to 120 hours, more preferably at least 3 hours, and 4 or more hours is even more preferable. It is preferable to select conditions by which the reaction completes at such conditions.
  • the pH of the reaction solution is not particularly limited so long as the reaction efficiently progresses; however, for example, it is a range of pH 4 to 10, and preferably pH 5.5 to 8.5.
  • methacrylic acid ester using methacrylyl-CoA transformed by action of ACD with isobutyryl-CoA as the raw material or methacrylyl-CoA transformed by action of ECH from 3-hydroxyisobutyryl-CoA, it is preferable to implement by adjusting so as to be in the range of these conditions.
  • the methacrylyl-CoA synthesis reaction from ACD or ECH can be conducted by a known method (for example, as reaction conditions for ACD, the conditions described in Microbiology (1999), 145, pp. 2323-2334). By combining with yet another biological reaction, continuous reaction (fermentative production) within an organism for methacrylic acid ester becomes possible.
  • the methacrylic acid ester formed by the method of the present invention can be qualitatively or quantitatively analyzed by way of gas chromatography (GC), high performance liquid chromatography (HPLC), or the like as necessary.
  • GC gas chromatography
  • HPLC high performance liquid chromatography
  • Isolation of methacrylic acid ester from the reaction solution can be performed by an individual or combination of known purification methods such as distillation, thin-film distillation, solvent extraction and column separation.
  • the obtained methacrylic acid ester can polymerize by a typical method, and used without inferiority in conventional uses.
  • the methacrylic acid ester obtained in this way or polymer thereof can remarkably reduce the energy, resources and load on the environment, and has an extremely great social value as a low-environmental load material compared to conventional chemicals with petroleum products as starting materials.
  • methacrylic acid ester from a precursor such as isobutyryl-CoA, 3-hydroxyisobutyryl-CoA or 2-isovaleric acid, by introducing ACD gene, ECH gene, BCKAD gene or the like as necessary to a microorganism to which AAT gene has been introduced.
  • Precursor indicates a compound that is inducible to methacrylyl-CoA, and indicates isobutyryl-CoA or 3-hydroxyisobutyryl-CoA, and further, the matter of a substance inducible to these two compounds.
  • the substance inducible to two compounds for example, acids such as 2-oxoisovaleric acid, isobutyric acid, 3-hydroxy isobutyric acid, acetic acid, pyruvic acid, lactic acid, acetoacetic acid, butyric acid, propionic acid, malic acid, fumaric acid, citric acid and succinic acid; amino acids such as valine, alanine, leucine, lysine and glutamic acid; and saccharides such as glucose, fructose and xylose can be exemplified.
  • methacrylic acid ester to form from these precursors, it is also possible to utilize various metabolic pathways naturally possessed by the host microorganism. Genes can be introduced or made deficient as necessary.
  • the host microorganism it is not particularly limited so long as being a host having enzymes for forming methacrylyl-CoA from the precursor and expression capability of AAT; however, as for bacterium, Rhodococcus, Pseudomonas, Corynebacterium, Bacillus, Streptococcus, Streptomyces , etc. can be exemplified, as for yeast, Saccharomyces, Candida, Shizosaccharomyces and Pichia , and as for filamentous fungus, Aspergillus , etc. can be exemplified.
  • a microorganism of Rhodococcus genus is preferable as the host. The reason thereof is because of the knowledge arrived at by experimentally confirming in the course of the present invention that a microorganism of Rhodococcus genus has valine assimilativity, and finding that, by utilizing this function, it is possible to apply to methacrylic acid ester formation by the route shown in FIG. 2 .
  • one type selected from the following microorganisms can be used individually, or by combining two or more types.
  • microorganisms classified as Rhodococcus sp. for example, Rhodococcus rhodochrous, Rhodococcus erythropolis, Rhodococcus equi, Rhodococcus rhodnii, Rhodococcus corallinus, Rhodococcus rubropertinctus, Rhodococcus coprophilus, Rhodococcus globerulus, Rhodococcus chlorophenolicus, Rhodococcus luteus, Rhodococcus aichiensis, Rhodococcus chubuensis, Rhodococcus maris, Rhodococcus fascines and the like can be exemplified.
  • Rhodococcus erythropolis can be exemplified.
  • Rhodococcus erythropolis strain PR-4 Rhodococcus erythropolis strain KA2-5-1, Rhodococcus erythropolis strain IGTS8, Rhodococcus erythropolis strain D-1, Rhodococcus erythropolis strain H-2, Rhodococcus erythropolis strain N1-36, Rhodococcus erythropolis strain 1-19, Rhodococcus erythropolis strain ECRD-1, Rhodococcus erythropolis strain B1, Rhodococcus erythropolis strain SY-1, Rhodococcus erythropolis strain UM3, Rhodococcus erythropolis strain UM9, Rhodococcus equi strain T09, or the like can be exemplified, and particularly preferably, Rhodococcus erythropolis strain PR-4 can be exemplified. Furthermore, derivatives of these strains are included.
  • variant strains obtained by inducing gene mutation in a microorganism having methacrylyl-CoA formability by way of a change in culture conditions (e.g., medium composition, temperature, etc.), chemical or physical treatment (e.g., ⁇ radiation, etc.), genetically modified strains for which activity has been enhanced in the following way, or activity has been made deficient or reduced are included.
  • Activity enhancement indicates the expression level of enzyme gene (irrespective of origin) increasing in the microorganism based on the gene introduced from outside the bacterial cell to the microorganism, and in addition to introducing genes encoding enzymes from outside the bacterial cell of the microorganism to inside the bacterial cell, includes enhancing the enzyme activity as a result of causing the enzyme gene to be highly expressed by enhancing the promoter activity of the enzyme gene retained on the genome by the microorganism, or substituting with another promoter, or alternatively, reducing or inactivating the repressor activity of the enzyme gene.
  • the genetically modified strain may be a modified strain arrived at by performing genetic modification causing the activity of enzyme inhibiting the methacrylyl-CoA synthesis reaction to be knocked out or decreased.
  • Activity “deficient” or “decrease” indicates the expression of the enzyme gene being entirely lost or reduced in this microorganism, and in addition to substitution, deletion or insertion occurring for this enzyme gene, includes decreasing the enzyme activity as a result of suppressing the expression of enzyme gene by decreasing the promoter activity of an enzyme gene retained on the genome by the microorganism or substituting with another promoter, or alternatively enhancing or activating the repressor activity of this enzyme gene. It should be noted that these genetic modifications may be performed following a conventional method.
  • a modified strain having at least one characteristic of (a) or (b) shown below can be exemplified.
  • the enzyme for forming methacrylyl-CoA from the precursor is selected as appropriate or optimized, and is not particularly limited; however, hereinafter, the necessary enzyme genes for methacrylic acid ester formation by the route shown in FIG. 2 will be described in detail using a microorganism of Rhodococcus genus as the host.
  • the AAT used in the present invention is not particularly limited so long as having ability to produce methacrylic acid ester with methacrylyl-CoA and alcohol or phenol as raw materials, and the kind and origin thereof are not of concern.
  • One of plant origin is preferable as the enzyme source, and as representative sources thereof, those originating from any order selected from the group consisting of the aforementioned Zingiberales, Rosales, Ericales, Cucurbitales, Brassicales and Laurales can be exemplified.
  • the ACD used in the present invention is not particularly limited so long as having an ability to form methacrylyl-CoA from acyl-CoA, and the source and type thereof are not of concern. Those derived from microorganism are preferable, and representative ones are as shown before.
  • Rhodococcus erythropolis is derived from Rhodococcus erythropolis , and as preferred strains, Rhodococcus erythropolis strain PR-4, Rhodococcus erythropolis strain KA2-5-1, Rhodococcus erythropolis strain IGTS8, Rhodococcus erythropolis strain D-1, Rhodococcus erythropolis strain H-2, Rhodococcus erythropolis strain N1-36, Rhodococcus erythropolis strain 1-19, Rhodococcus erythropolis strain ECRD-1, Rhodococcus erythropolis strain B1, Rhodococcus erythropolis strain SY-1, Rhodococcus erythropolis strain UM3, Rhodococcus erythropolis strain UM9, Rhodococcus equi strain T09, or the like can be exemplified, and particularly preferably, Rhodococcus erythropolis strain PR-4 can be exemplified.
  • the nucleotide sequence of ACD gene derived from Rhodococcus erythropolis strain PR-4 is shown in SEQ ID NO. 33, and the amino acid sequence coded by this nucleotide sequence is shown in SEQ ID NO. 32. It should be noted that amino acid sequences in which one or a plurality of amino acids in the amino acid sequence shown in SEQ ID NO. 32 have been substituted, deleted or added are included, and genes coding proteins having activity to form methacrylyl-CoA from acyl-CoA are also included in the ACD gene of the present invention.
  • genes hybridizing under stringent conditions to a polynucleotide having the complementary nucleotide sequence to the nucleotide sequence shown by SEQ ID NO. 33, and coding proteins having activity to form methacrylic acid ester from acyl-CoA are also included.
  • genes hybridizing under stringent conditions to a polynucleotide having the complementary nucleotide sequence to the nucleotide sequence shown by SEQ ID NO. 33 and coding proteins having activity to form methacrylic acid ester from acyl-CoA are also included.
  • when calculating using the nucleotide sequence shown in SEQ ID NO. 33, BLAST, etc. e.g., default, i.e.
  • genes coding proteins having activity to form methacrylic acid ester from acyl-CoA and alcohol consisting of a nucleotide sequence having identity of at least 80%, more preferably at least 90%, and most preferably at least 95% are also included.
  • the codons of the above-mentioned ACD gene may be changed according to the codon frequency of use in the microorganism used in transformation.
  • DNA coding the above-mentioned AAT gene and/or ACD gene is introduced to a microorganism belonging to Rhodococcus sp., and used to cause transcription/translation to proteins in this microorganism.
  • the DNA introduced to this microorganism is preferably in the form incorporated in a vector.
  • DNA coding the above-mentioned AAT gene and/or ACD gene is introduced to the host microorganism, and used to cause transcription/translation to proteins in this microorganism.
  • the DNA introduced to this microorganism is preferably in the form incorporated in a vector.
  • each gene is incorporated into an expression vector that can be expressed by the host cell, and this is introduced to the host cell.
  • the vector is not particularly limited so long as being autonomously replicable in the host cell, and retaining the AAT gene and/or ACD gene, and it is possible to use vectors suited to the respective microorganisms.
  • the vector for introducing DNA to microorganism belonging to Rhodococcus sp. for example, it is possible to use well-known vectors such as pK1, pK2, pK3 and pK4, as well as pSJ034 (refer to Japanese Unexamined Patent Application, Publication No. H10-337185), pSJ023 and pSJ002 (refer to Japanese Unexamined Patent Application, Publication No. H10-24867), and pSJ201 and pLK005 (not limited to these).
  • pSJ023 is deposited in the National Institute of Advanced Industrial Science and Technology, Patent Organism Depository as transformant Rhodococcus rhodochrous ATCC12674/pSJ023 (FERMBP-6232).
  • the insertion of the above-mentioned AAT gene and/or ACD gene to the vector can be carried out using gene recombination technology known to those skilled in the art. For example, it is possible to utilize a method using restriction enzyme cleavage and ligation, a method using topoisomerase, an In Fusion kit (Takara Bio), and the like.
  • the gene inserted into the vector is inserted successively downstream of a promotor capable of regulating transcription/translation of proteins encoded by the respective genes in the host organism.
  • an appropriate linker may be added upon insertion.
  • a terminator sequence, enhancer sequence, splicing signal sequence, polyA addition signal sequence, ribosome-binding sequence such as the SD sequence or Kozak sequence, selection marker gene, etc. usable in the host organism into which genes are trying to be introduced can be linked.
  • the selection marker gene in addition to drug resistant genes such as ampicillin-resistant gene, tetracycline-resistant gene, neomycin-resistant gene, kanamycin-resistant gene and chloramphenicol-resistant gene, genes imparting intracellular biosynthesis of nutrients such as amino acids and nucleic acids, or genes coding fluorescent proteins such as luciferase can be exemplified. Accompanying insertion, a part of the amino acid sequence coded by the DNA may be substituted.
  • pLK005 acquired by performing variation treatment on pK4 as the vector.
  • the AAT gene or ACD gene is linked/inserted so as to be disposed downstream of 3′ of the promoter of pLK005, and an expression plasmid vector that expresses AAT gene and/or ACD gene can be constructed by the promoter.
  • any gene selected from the AAT gene cluster or ACD gene cluster may be inserted, and a plurality of genes may be inserted.
  • “plurality” can be inserting 2 to 5, 2 to 4, and preferably 2 or 3 genes.
  • these genes preferably form an operon.
  • “operon” is a nucleic acid sequence unit constituted from one or more genes transcribed under the control of the same promoter.
  • the above-mentioned genes, and preferably genes in the form of a vector, are inserted to the host microorganism by a method known to those skilled in the art.
  • the introduction method of the recombinant vector to the host organism is not particularly limited so long as being a method suited to the host microorganism and, for example, the electroporation method, spheroplast method, lithium acetate method, calcium phosphate method, lipofection method, conjugational transfer method and the like can be exemplified.
  • the recombinant microorganism to which the required genes such as AAT gene and/or ACD gene are introduced is brought into contact with the precursor to produce methacrylic acid ester.
  • contact indicates exposure treating for a fixed time the microorganism and a substance (precursor). More specifically, the microorganism is cultured in an aqueous medium containing precursor (raw material), etc., or a culture of the microorganism is added to the aqueous medium containing raw material, and suspended/mixed, to obtain methacrylic acid ester in the aqueous medium and/or gas phase. Upon doing so, it is of no concern if there is proliferation of microorganism. In this process, a mixture containing recombinant microorganism, and methacrylic acid ester is obtained.
  • “Aqueous medium” indicates water or an aqueous solution with water as a principle component, and also includes those in which undissolved liquid/solid are dispersed.
  • “Gas phase” refers to a portion occupied by gas, steam, etc. excluding a portion occupied by liquid (culture medium, etc.) in the culture tank (vessel culturing microorganism) or reactor (vessel carrying out reaction).
  • “Culture” indicates that obtained by way of a culturing of bacterial cells, broth, noncellular extract, cellular membrane, or the like.
  • production of methacrylic acid ester is performed by causing methacrylic acid ester to be form and accumulate in culture bacterial cells or the culture by culturing gene recombinant microorganism to which AAT gene has been introduced in an aqueous medium containing the precursor, and recovering the methacrylic acid ester from the culture bacterial cell, culture or culture vessel gas phase.
  • the culture medium used in the culturing of microorganism is a solid medium or liquid medium enabling sufficient proliferation that contains nutrients at least including various carbon sources.
  • precursor being usable as the carbon source, it can be used as the carbon source.
  • the concentration of carbon source or precursor in the culture medium is not particularly limited so long as enabling the production of methacrylic acid ester.
  • the concentration for example, is set to 0.05 to 20 (w/v) %, preferably 0.1 to 15 (w/v) %, and more preferably 0.2 to 10 (w/v) %. At least 0.2 (w/v) % is used because the methacrylic acid productivity of microorganisms increases, and it is set to no more than 10 (w/v) % because a dramatic improvement in effect is not recognized even if increasing to more than this.
  • alcohol or phenol is added depending on the target methacrylic acid ester.
  • the alcohol or phenol used is preferably one shown by Formula 2.
  • the concentration of alcohol or phenol in the culture medium is not particularly limited so long as enabling methacrylic acid ester to be produced.
  • the concentration for example, is set to 0.01 to 20 (w/v) %, preferably 0.05 to 10 (w/v) %, and more preferably 0.1 to 5 (w/v) %.
  • these can also be added to the culture medium in advance, or can be added continuously or intermittently by dividing into two or more occurrences, while performing culturing.
  • inorganic nitrogen sources inorganic metal salts or the like may be added.
  • inorganic nitrogen sources for example, inorganic acids or organic acids of ammonium salts such as ammonium chloride, ammonium sulfate, ammonium acetate and ammonium phosphate, and the like can be used.
  • the concentration of nitrogen source in the culture medium is not particularly limited so long as enabling methacrylic acid ester to be produced.
  • the concentration for example, is set to 0.01 to 10 (w/v) %, preferably 0.05 to 8 (w/v) %, and more preferably 0.1 to 4 (w/v) %.
  • potassium dihydrogen phosphate potassium monophosphate
  • magnesium phosphate magnesium sulfate
  • sodium chloride ferrous sulfate
  • manganese sulfate copper sulfate, calcium carbonate, etc.
  • inorganic metal salts for example, potassium dihydrogen phosphate, potassium monophosphate, magnesium phosphate, magnesium sulfate, sodium chloride, ferrous sulfate, manganese sulfate, copper sulfate, calcium carbonate, etc.
  • the concentration of inorganic salts in the culture medium is not particularly limited so long as enabling methacrylic acid ester to be produced.
  • the concentration for example, is set to 0.001 to 1.6 (w/v) %, preferably 0.005 to 1.3 (w/v) %, and more preferably 0.01 to 1 (w/v) %.
  • At least 0.1 (w/v) % is used because the methacrylic acid productivity of microorganisms increases, and it is set to no more than 1 (w/v) % because a dramatic improvement in effect is not recognized even if adding more than this.
  • trace metals, vitamins, etc. are added as necessary to the culture medium.
  • various organic substances, inorganic substances, surfactant, commonly used defoaming agent, etc. necessary in the breeding of the microorganism can be additionally added to the culture medium as necessary.
  • Seeding of the genetically modified microorganism to the culture medium may be carried out by a conventional, known technique.
  • the culture method also is not particularly limited, and it is possible to use a known technique such as shaking culture, aerated and agitated culture, and static culture.
  • the culturing conditions are not particularly limited so long as the genetically modified organism breeds and forms methacrylic acid ester. Culturing may be carried out under aerobic conditions or may be carried out under anaerobic conditions.
  • the pH, temperature and culturing time are not particularly limited so long as conditions allowing the genetically modified microorganism to breed and form methacrylic acid ester.
  • the pH is preferably set to 3 to 10, more preferably 4 to 9, and even more preferably 5 to 8.
  • the temperature is preferably set to 10 to 45° C., more preferably 15 to 40° C., and even more preferably 20 to 35° C.
  • the culturing time is preferably 10 to 1000 hours, more preferably 15 to 480 hours, and even more preferably 20 to 240 hours.
  • culturing conditions are appropriately selected or optimized for every strain so as to maximize the ratio of yield of methacrylic acid ester relative to the utilized amount of carbon source or precursor. It should be noted that the yield of methacrylic acid ester can be adjusted by appropriately adjusting the amount of carbon source and culturing conditions.
  • the concentration of carbon source or precursor in the culture medium is directly or indirectly maintained to at least 0.1%
  • the concentration of alcohol or phenols is directly or indirectly maintained to at least 0.1%
  • the temperature is adjusted to the range of 20 to 40° C., and allowed to react for at least 3 hours.
  • the concentration of microorganism in the culture solution is high in a range in which the environment of the culture solution does not become inappropriate for proliferation of the microorganism or cultured cells and the ratio of cells dying does not rise and, for example, by maintaining in at least 2 g/L as a dry weight, favorable production efficiency is obtained, and the accumulation concentration of production can be raised.
  • the following method can be employed in addition to the method by culturing genetically modified microorganism as described above.
  • the genetically modified microorganism does not need to have reproductive activity, and a precultured culture can be brought into contact with an aqueous medium containing precursor to produce methacrylic acid ester by resting microorganism reaction unaccompanied by substantial proliferation.
  • the concentration of the precursor used in resting microorganism reaction may be the same as the above-mentioned case of production of methacrylic acid ester from culturing.
  • the alcohol or phenol used in resting microorganism reaction and the concentration thereof may be the same as the above-mentioned case of production of methacrylic acid ester by culturing.
  • Inorganic metal salts, etc. may be added to the reaction solution.
  • inorganic metal salts for example, potassium dihydrogen phosphate, potassium monophosphate, magnesium phosphate, magnesium sulfate, sodium chloride, ferrous sulfate, manganese sulfate, copper sulfate, calcium carbonate, etc. can be used.
  • the concentration of inorganic salts in the reaction solution is not particularly limited so long as enabling methacrylic acid ester to be produced.
  • the concentration for example, is set to 0.0001 to 2 (w/v) %, preferably 0.0003 to 1.3 (w/v) %, and more preferably 0.001 to 1 (w/v) %.
  • the culture solution of precultured genetically modified microorganism is used as is, or bacterial cells recovered by filtering, centrifuging or the like are used.
  • the recovered culture is resuspended in an appropriate buffer solution or the like, and can be used by establishing in any bacteria concentration.
  • a normal saline solution, potassium phosphate buffer solution, tris-hydrochloric acid buffer solution, glycine-sodium hydroxide buffer solution, boric acid-sodium hydroxide buffer solution, or the like is used for the buffer solution or the like.
  • the processed product of the recovered culture e.g., homogenate, crude enzyme, purified enzyme, etc.
  • it may be fixed to an appropriate carrier by a known method, and this fixation product may be used in reaction.
  • the reaction conditions are not particularly limited so long as forming methacrylic acid ester.
  • the reaction may be carried out under aerobic conditions or may be carried out under anaerobic conditions.
  • the reaction method is also not particularly limited, and a well-known technique such as shaking reaction, aerated and agitated reaction, and static reaction can be used.
  • the pH, temperature and reaction time are not particularly limited so long as conditions that can form methacrylic acid ester.
  • the pH is preferably set to 3 to 10, more preferably 4 to 9, and even more preferably 5 to 8.
  • the temperature is preferably set to 10 to 45° C., more preferably 15 to 40° C., and even more preferably 20 to 35° C.
  • the reaction time is preferably 5 to 180 hours, more preferably 10 to 150 hours, and even more preferably 15 to 120 hours.
  • reaction conditions are appropriately selected or optimized for every strain so as to maximize the ratio of yield of methacrylic acid ester. It should be noted that the yield of methacrylic acid ester can be adjusted by appropriately adjusting the reaction conditions.
  • the concentration of carbon source or precursor in the culture medium is directly or indirectly maintained to at least 0.1%
  • the concentration of alcohol or phenols is directly or indirectly maintained to at least 0.1%
  • the temperature is adjusted to the range of 20 to 40° C., and allowed to react for at least 3 hours.
  • maintaining a state in which the concentration of microorganism in the reaction solution is high is preferable to obtain efficient productivity, and for example, by maintaining in at least 2 g/L as a dry weight, favorable production efficiency is obtained, and the accumulation concentration of product can be improved.
  • the aforementioned production of methacrylic acid ester from culturing and the production of methacrylic acid ester from resting microorganism reaction may be carried out by combining as appropriate. By combining the two methods, the more efficient production of methacrylic acid ester becomes possible.
  • the methacrylic acid ester formed in the culture medium or reaction solution and the formed amount thereof can be detected and measured using a common method such as of high-performance liquid chromatography and LC-MS.
  • the methacrylic acid ester volatilized in the gas phase of the culture container or reaction container (head space part) and formed amount thereof can be detected and measured using a common method such as gas chromatography.
  • the methacrylic acid ester can be separated and purified from the culture medium or reaction solution using an appropriate combination, as necessary, of well-known operations such as filtration, centrifugation, vacuum concentration, ion exchange or adsorption chromatography, solvent extraction, distillation and crystallization.
  • the skin of a banana was removed, the sarcocarp was sliced to about 1 millimeter thickness with a cutter, and this was further divided into four.
  • Two grams of sliced banana, 2 ml of a solution containing 2.3 mM methacrylyl-CoA and 0.35 M of KCl and 5 ⁇ l of isobutyl alcohol were added in order to a 100 ml flask. It was sealed and allowed to react at 30° C.
  • the reaction mixture containing Isobutyl methacrylate formed after 1, 2 or 3 hours was collected in a 100 ml flask with 150 ⁇ l of head space, and analysis was performed with the GC conditions below. The results thereof are shown in Table 1.
  • concentration of methacrylic acid ester was calculated by adjusting an aqueous solution of a known initial concentration, placing 2 ml of the same aqueous solution in a 100 ml flask, and after incubating for 30 min at 30° C., collecting the head space by the same method, subjecting to GC analysis, and preparing a calibration curve.
  • E. coli JM109 was innoculated in 1 mL of LB medium (1% Bacto tryptone, 0.5% Bacto yeast extract, 0.5% NaCl), precultured aerobically at 37° C. for 5 hours, 0.4 mL of the culture was added to 40 mL of SOB medium (2% Bacto tryptone, 0.5% Bacto yeast extract, 10 mM NaCl, 2.5 mM KCl, 1 mM MgSO 4 , 1 mM MgCl 2 ), and was cultured at 18° C. for 20 hours.
  • LB medium 1% Bacto tryptone, 0.5% Bacto yeast extract, 0.5% NaCl
  • SOB medium 2% Bacto tryptone, 0.5% Bacto yeast extract, 10 mM NaCl, 2.5 mM KCl, 1 mM MgSO 4 , 1 mM MgCl 2
  • the plant-derived AAT genes shown in SEQ ID NOS: 2, 4 and 6 were entrusted for synthesis by Takara Bio Inc. Apple AAT
  • Strawberry AAT amino acid sequence (SEQ ID NO: 5), nucleotide sequence (SEQ ID NO: 6)
  • MMA-044 5′-GTTTGCACGCCTGCCGTTCGACG-3′
  • MMA-045 5′-CGGTACGCGCGGATCTTCCAGAG-3′ Reaction Solution Composition
  • a band of obtained amplification product was purified by a QIAquick Gel Extraction Kit (QIAGEN).
  • the respective purified DNA was digested with restriction enzyme PagI (cleavage recognition site included in Forward Primer) and Sse8387I (cleavage recognition site included in Reverse Primer). Separation was performed by agarose gel electrophoresis, the target band was excised from the gel, and purification was performed.
  • purification using a Gel/PCR Purification Kit (manufactured by FAVORGEN), it was eluted to 30 ⁇ L of sterile water.
  • the purified DNA (5 ⁇ L), vector pTrc99A digested with NcoI and Sse8387I (1 ⁇ L), distilled water (4 ⁇ L) and solution I (DNA Ligation Kit ver. 2 (Takara Bio)) (10 ⁇ L) were mixed, and the vector was ligated with PCR amplification product by incubating for 12 hours at 16° C.
  • LBAmp nutrient agar LB culture medium containing 100 mg/L ampicillin, 1.5% agar
  • a plurality of transformant colonies grown on nutrient agar was cultured overnight at 37° C. in 1.5 mL of LBAmp culture medium (LB culture medium containing 100 mg/L ampicillin), and after harvesting, plasmid DNA was prepared using a QIAprep Spin Miniprep kit (QIAGEN).
  • the nucleotide sequence thereof was confirmed using a CEQ DTCS Quick Start Kit and fluorescent sequencer CEQ 2000XL DNA Analyzer (both Beckman Coulter, USA), and were named plasmid pAAT101 to pAAT103 (Table 6).
  • pAAT201 For the pET16b vectors, AAT gene was introduced by similar operations, and the obtained plasmids were named pAAT201 to pAAT203 (Table 6). However, since there is no Sse8387I site in pET16b, that in which a linker including the Sse8387I cleavage sequence had been inserted at the BamHI site of pET16b was prepared in advance, and this was used as a vector.
  • the plasmids pAAT101 to pAAT103 were introduced to JM109 strain to obtain recombinant JM109/pAAT101 to pAAT103.
  • the plasmids pAAT201 to pAAT203 were introduced to the BL21(DE3) strain to obtain recombinant BL21(DE3)/pAAT201 to pAAT203.
  • the Recombinant E. colis JM109/pAAT101 to pAAT103 obtained in Example 6 were inoculated into 1 ml of an LB culture medium containing 100 ⁇ g/ml of ampicillin, and preculturing was performed at 37° C. for 7 hours.
  • the broth was taken in 0.1 ml, added to 100 ml of the same culture medium (100 ⁇ g/ml ampicillin, 1 m MIPTG contained), and shaking cultured at 37° C. for 15 hours.
  • the bacterial cell was recovered by way of centrifugation (3,700 ⁇ g, 10 min, 4° C.) from the obtained broth, and after washing with a 10 mM sodium phosphate buffer solution (pH 7.0), was suspended in the same buffer solution.
  • JM109/pTrc99A was used as a reference strain.
  • the recombinant E. colis BL21(DE3)/pAAT201 to pAAT203 obtained in Example 6 were inoculated into 1 ml of an LB culture medium containing 100 ⁇ g/ml of ampicillin, and preculturing was performed at 37° C. for 14 hours.
  • the broth was taken in 0.1 ml, added to 100 ml of the same culture medium (100 ⁇ g/ml ampicillin), and after shaking cultured at 37° C. until the OD became 0.3, IPTG was added so that the final concentration became 1 mM and was further shaking cultured for several hours.
  • BL21(DE3)/pET16b was used as a reference strain.
  • the following reaction was performed using cell-free extract prepared by the method described in Example 7.
  • the reaction was initiated by adding 0.2 ml of cell-free extract to a 10 ml-sample bottle with a septum (for GC) into which 0.8 ml of a solution of methacrylyl-CoA and alcohol was placed so that the final concentration of the reaction solution was 7 mM methacrylyl-CoA and 40.5 mM n-butanol.
  • the sample bottle with a septum was incubated at 30° C. for 1 to 5 hours to cause reaction.
  • the reaction was initiated by adding 0.2 ml of cell-free extract to a 10 ml-sample bottle with a septum (for GC) into which 0.8 ml of a solution containing methacrylyl-CoA and alcohol was placed so that the final concentration of the reaction solution was 1 mM methacrylyl-CoA and 40 mM n-butanol.
  • Methacrylic Acid Esters (Isobutyl Methacrylate, Phenyl Methacrylate, Benzyl Methacrylate, 2-Ethylhexyl Methacrylate) Using AAT Gene Recombinant
  • Pseudomonas aeruginosa PAO1 strain (NBRC106052) grown on LB nutrient agar (1% Bacto tryptone, 0.5% Bacto yeast extract, 0.5% NaCl, 1.5% agar) was inoculated to 10 ml of LB liquid culture medium (1% Bacto tryptone, 0.5% Bacto yeast extract, 0.5% NaCl), and shaking culturing was performed at 37° C. for 15 hours. After culturing completion, the bacterial cell was recovered by way of centrifuge from 2 ml of the broth, and 100 ⁇ l of genomic DNA was prepared using a Wizard Genomic DNA Purification Kit (Promega KK).
  • the obtained genomic DNA was made a template, and a DNA fragment including a gene assumed to code ACD was prepared by way of the PCR method so as to be a form in which a restriction endonuclease recognition site enabling easy introduction to an expression vector was added.
  • MMA-003 5′-GACCCATGGATTTCGACCTCACCGAAGAAC-3′
  • MMA-004 5′-GCCCTGCAGGATGCGATGGTTCGCGGCGTTC-3′ Reaction Solution Composition
  • MMA-003 (SEQ ID NO. 13) 1 ⁇ l
  • MMA-004 (SEQ ID NO. 14) 1 ⁇ l
  • a band of about 1.2 kb of the obtained amplification product was purified by a QIAquick Gel Extraction Kit (QIAGEN).
  • the purified DNA was digested with digested with restriction enzyme NcoI (cleavage recognition site included in oligonucleotide MMA-003) and Sse8387I (cleavage recognition site included in oligonucleotide MMA-004), and purified by way of phenol extraction/chloroform extraction/ethanol precipitation.
  • the purified DNA (5 ⁇ L), vector pTrc99A digested with NcoI and Sse8387I (1 ⁇ L), distilled water (4 ⁇ L) and solution I (DNA ligation Kit ver. 2 (Takara Bio)) (10 ⁇ L) were mixed, and the vector was ligated with PCR amplification product by incubating for 12 hours at 16° C.
  • LBAmp nutrient agar LB culture medium containing 100 mg/L ampicillin, 1.5% agar
  • a plurality of transgenic organism colonies cultured on nutrient agar was cultured overnight at 37° C. in 1.5 mL of LBAmp culture medium (LB culture medium containing 100 mg/L ampicillin), and after harvesting, plasmid DNA was recovered using a Flexi Prep (manufactured by Amersham Biosciences).
  • the nucleotide sequence thereof was confirmed using a CEQ DTCS Quick Start Kit and fluorescent sequencer CEQ 2000XL DNA Analyzer (both Beckman Coulter, USA), and was named plasmid pMMA002.
  • the E. coli JM109 strain was transformed using the plasmid pMMA002 to prepare a recombinant to which the ACD gene (SEQ ID NO. 8) had been introduced.
  • the amino acid sequence is shown by SEQ ID NO. 7.
  • Recombinant E. coli JM109/pMMA002 to which the ACD gene (SEQ ID NO. 8) obtained in Example 10 had been introduced was inoculated to 1 ml of an LB culture medium containing 100 ⁇ g/ml ampicillin, and preculturing was performed at 37° C. for 7 hours.
  • the broth was taken in 0.1 ml, added to 100 ml of the same culture medium (100 ⁇ g/ml ampicillin, 1 m MIPTG contained), and shaking cultured at 37° C. for 15 hours.
  • Reaction solution diluted 10 times with mobile phase and measured.
  • the skin of a banana was removed, the sarcrocarp was sliced with a cutter to a thickness of about 1 millimeter, and this was further divided into four.
  • To a 50-ml flask 1 g of the sliced banana, 0.9 ml of the methacrylyl-CoA synthesis reaction solution, 0.1 ml of 3.5 M KCl solution and 5 ⁇ l of n-butyl alcohol were added, sealed, and then allowed to react at 30° C. for 2 hours.
  • methacrylic acid ester similarly to Example 1, 0.015 mM of butyl methacrylate formed.
  • Rhodococcus erythropolis PR4 strain (NBRC100887) grown on LB nutrient agar culture medium was inoculated to 10 mL of LB liquid culture medium, and shaking culturing was performed at 30° C. for 36 hours. After culturing completion, the bacterial cell was recovered by way of centrifuge from 2 ml of the broth, and 100 ⁇ l of genomic DNA was acquired similarly to Example 10.
  • the obtained genomic DNA was made a template, and a DNA fragment including a nucleotide sequence assumed to encode ECH gene was prepared by way of the PCR method so as to be a form in which a restriction endonuclease recognition site enabling easy introduction to an expression vector is added.
  • MMA-031 5′-GGTCATGACCGACTTCAACACCATCATCCTC-3′
  • MMA-032 5′-GGCCTGCAGGTTCAGCTGTTCGAAAGTTCAGCGC-3′
  • PCR was performed similarly to Example 10, and the obtained DNA was digested with restriction enzyme BspHI (cleavage recognition site included in oligonucleotide MMA-031) and Sse8387I (cleavage recognition site included in oligonucleotide MMA-032). After cleavage, the same operations as Example 6 were performed to acquire the target plasmid DNA to which ECH gene (SEQ ID NO. 10) was incorporated, and then named plasmid pMMA011. The amino acid sequence is shown by SEQ ID NO. 9.
  • E. coli JM109 strain was transformed using plasmid pMMA011 to prepare ECH gene expression Recombinant E. coli.
  • the Recombinant E. coli JM109/pMA011 to which the ECH gene obtained in Example 13 had been introduced was inoculated in an LB culture medium containing 2 ml of 100 ⁇ g/ml ampicillin, and preculturing was performed at 37° C. for 24 hours.
  • the broth was taken in 0.1 ml, added to 100 ml of the same culture medium (100 ⁇ g/ml ampicillin, 1 m MIPTG contained), and shaking cultured at 37° C. for 15 hours.
  • the Recombinant E. coli JM109/pWA108 obtained in the above way was cultured similarly to Example 10. However, in the case of the present recombinant, since high expression of protein was recognized even without performing addition of IPTG based on the preliminary results, it was conducted without the addition of IPTG. The preparation of cell-free extract was conducted similarly to Example 11.
  • the BCKAD activity was measured from the generation of isobutyryl-CoA with 2-oxoisovaleric acid as the substrate in the following way.
  • Example 15 To 0.7 ml of a solution containing final concentrations of 1 mM MgCl 2 , 0.2 mM thiamin pyrophosphate, 1 mM CoA-Sh and 2 mM DDT in a 100 mM sodium phosphate buffer solution (pH 7.0), 0.2 ml of the cell-free extract obtained in Example 15 was added to make up 0.9 mL. After adding 0.1 mL (4 mM final concentration) of 2-oxoisovaleric acid calcium salt to this and reacting at 37° C. for 30 minutes, ultrafiltration was performed using a Centricut Super Mini W-10 (Kurabo Industries Ltd.). The reaction was stopped by performing deproteinization, and analysis was performed by HPLC at the following conditions. As a result thereof, the formation of 0.83 mM isobutyryl-CoA was recognized with JM109/pWA108.
  • Injection volume 10 ⁇ l (reaction solution diluted 10 times with mobile phase and measured)
  • Example 17 Synthesis of Methacrylyl-CoA (FIG. 1 ) from 2-Oxoisovaleric Acid by Cell-Free Extract Mixture from BCKAD Gene High-Expression Recombinant and Recombinant Expressing ACD Gene
  • Rhodococcus erthropolis PR4 (NITE Biological Resource Center; deposit number: NBRC 100887) was modified by the method described in Japanese Unexamined Patent Application, Publication No. 2011-200133 to prepare a derivative exhibiting resistance to 120 mg/L chloramphenicol and lacking kanamycin-resistant gene, and was named as PR4KS strain.
  • the concentration of chloramphenicol in an MYK culture medium (0.5% polypeptone, 0.3% bact-yeast extract, 0.3% malt extract, 0.2% KH 2 PO 4 , 0.2% K 2 HPO 4 ) was gradually raised step-wise starting from 10 mg/mL until 120 mg/mL, while inducing spontaneous mutation by subculturing PR4 strain, thereby obtaining derivative RhCmSR-09 strain having resistance to 120 mg/mL of chloramphenicol.
  • RhCmSR-09 strain was mixed at a 1:1 ratio with E. coli retaining the plasmid pKM043 for the kanamycin-resistant gene deficiency variation introduction described in Japanese Unexamined Patent Application, Publication No.
  • the homologous recombinant strain was cultured in 10% sucrose-containing MYK nutrient agar, whereby a derivative strain emerging as a kanamycin-sensitive strain from among the obtained colonies, i.e. kanamycin-resistant gene deficiency variation derivative strain PR4KS, was obtained.
  • the LigD homolog gene (accession No: YP_002767969) of the PR4KS strain was established as the target gene. After amplification of about 5.4 kb of DNA including the LigD homolog gene surrounding sequence by way of PCR, it was cloned to plasmid vector pK19mobsacB1 to which the sacB gene had been introduced downstream and in the same orientation of the kanamycin-resistant gene, described in Japanese Unexamined Patent Application, Publication No. 2011-200133, thereby obtaining plasmid pTJ001.
  • the PCR conditions were as follows.
  • GB-138 5′-GGCCTGCAGGTACCGATCATCACCATCGGTGTC-3′ (SEQ ID NO. 20)
  • GB-139 5′-GGTCTAGACTGAGCAGTGTTCCAATGCG-3′ Reaction Solution Composition
  • PR4KS genome 50 ng/ ⁇ L 1 ⁇ l
  • the plasmid for LigD homolog gene deficiency pTJ002 was prepared in which the entire length of the LigD homolog sequence inside pTJ001 (about 2.3 kb) was deleted and only the upstream and downstream sequences of the LigD homolog gene were allowed to remain (refer to FIG. 3 ).
  • the sequence within pTJ001 was amplified using primers GB-140 and GB-141, which include the surrounding sequence of the start codon and the surrounding sequence of the stop codon of the targeted LigD homolog gene, respectively, and which were designed so as to extend in the upstream direction from the start codon and in the downstream direction of the stop codon, respectively, in order to obtain PCR product that does not include the LigD homolog gene.
  • E. coli JM109 strain was transformed by the obtained PCR product to make circular DNA as pTJ002.
  • the PCR conditions are as follows.
  • GB-140 GAGGAAATGGTCACAGGGCGAGAATAGGTTG (SEQ ID NO. 22)
  • GB-141 GCCCTGTGACCATTTCCTCATTGTGCTGG Reaction Solution Composition
  • plasmid pTJ002 After PCR completion, upon performing confirmation of the fragment by 0.7% agarose gel electrophoresis using 1 ⁇ l of sample, amplification of the fragment was recognized.
  • a Wizard Genomic DNA Purification Kit (manufactured by Promega) was used in the genome extraction from PR4 strain
  • a Gel/PCR Purification Kit (manufactured by FAVORGEN) was used in the purification of DNA fragment digested with the restriction enzyme and the PCR product
  • a DNA Ligation Kit ⁇ Mighty Mix> (manufactured by Takara Bio) was used in the joining of DNA
  • QIAprep miniprep kit (manufactured by QIAGEN) was used in the extraction of plasmid.
  • Rhodococcus sp N775 (National Institute of Advanced Industrial Science and Technology, Patent Organism Depository, deposit number FERM BP-961) was transformed by the above-mentioned electroporation method.
  • the obtained transformant was inoculated to 10 ml of MYK culture medium, and cultured at 30° C. for 1 day.
  • Variation treatment was performed by exposing this to ultraviolet light inside a clean bench.
  • the culture liquid in which variation treatment was performed was applied to MYK nutrient agar containing 50 to 400 ⁇ g/ml kanamycin, and cultured at 30° C. for 3 days.
  • the plurality of colonies appearing on the nutrient agar was respectively cultured in MYK culture medium, and plasmids were recovered from the transformants. Using the recovered plasmid, Rhodococcus sp N775 was transformed again, and it was investigated whether the kanamycin resistance of the transformant improves. As a result thereof, a number of strains of transformant for which the kanamycin resistance clearly improved were recognized.
  • the plasmid pSJ034 is a plasmid prepared from the plasmid pSJ023 by the method described in Japanese Unexamined Patent Application, Publication No. H10-337185.
  • pSJ034 although three EcoRI restriction enzymes sites are present, the plasmid pSJ040 was prepared in which one of these was transformed to a SpeI site.
  • pSJ034 was partially decomposed using restriction enzyme EcoRI. The cleavaged site was converted into blunt end using Takara Blunting kit and then ligation reaction was performed under the presence of SpeI linker. E. coli JM109 strain was transformed using the reaction solution.
  • pLK005 was digested with HindIII to prepare a fragment of about 2.1 kb.
  • pSJ040 was digested with HindIII to prepare a fragment of about 9.8 kb.
  • the ligation reaction was performed, and E. coli JM109 strain was transformed using the reaction solution.
  • the plasmid was extracted and the nucleotide sequence thereof was confirmed, a result of which a plasmid keeping the mutated sequence (duplication of GTTGTAGG) derived from pLK005, and otherwise having the same sequence as pSJ040 was named pSJ201.
  • the preparation of a plasmid for gene deficiency was performed by way of an In-Fusion HD Cloning kit (manufactured by Takara Bio) in which the RE_acd1/RE_echA/RE_hchA/RE_mmsB gene of PR4KS strain was the target gene (refer to FIG. 4 ).
  • the DNA of the upstream and downstream sequences of the target gene was amplified by PCR.
  • the PCR conditions were as follows.
  • MMA-061 CGACTCTAGAGGATCGCTCAGTACATCTACGAGAC (SEQ ID NO. 24)
  • MMA-062 AGTGTGAGGAAAGTGTTCCGATCAGTTCAT Primers for Fragment 2
  • MMA-063 CACTTTCCTCACACTCGTCGAGAGTATGAG (SEQ ID NO. 26)
  • MMA-064 CGGTACCCGGGGATCAGCGCGACGAACAACGAGAC Reaction Solution Composition
  • the linkage of the above-mentioned fragment and vector was performed using the In-Fusion HD Cloning Kit.
  • the reaction conditions were as follows.
  • E. coli JM109 strain After incubating the above-mentioned reaction solution at 50° C. for 15 minutes, it was cooled on ice, and used in the transformation of E. coli JM109 strain.
  • the selection of E. coli transformant was performed with LB nutrient agar containing 50 mg/L kanamycin sulfate (hereinafter, LB Km 50 nutrient agar). Plasmid was prepared from the obtained transformant using a Mini prep Kit (QIAGEN) to obtain the target plasmid. Confirmation of the plasmid was performed by investigating the fragment size after XbaI restriction enzyme treatment, and the sequence of the linkage region of the insert fragment and vector.
  • the target plasmid was named pMMA302.
  • MMA-069 GCGCATCTACAAGGAAGAGATC (SEQ ID NO. 28)
  • MMA-070 GCGACGCTCATCGAGATCTC Reaction Solution Composition
  • the colony recognized as being a homologous recombinant derivative strain was suspended in 200 ⁇ l of LB culture medium, 100 ⁇ l was spreadon LB+10% sucrose nutrient agar, and cultured for 3 days. From the grown colonies, those that came to be kanamycin sensitive were selected, and the target gene deficiency was confirmed for these by colony PCR. As a result thereof, a strain in which the four genes of RE_acd1, RE_echA, RE_hchA and RE_mmsB had been deleted from the PR4KS ⁇ ligD derivative strain was obtained, and named DMA008 strain.
  • Example 18 Preparation of Plasmid for ACD and AAT Co-Expression in Microorganism Belonging to Rhodococcus Genus
  • Plasmid for expressing ACD and/or AAT in microorganisms belonging to Rhodococcus genus was prepared.
  • a “nitrilase promoter+MpAAT1 gene” fragment obtained by PCR reaction with plasmid pAAT301 for MpAAT1 gene expression as the template was inserted downstream of the RE_acd1 gene of plasmid pMMA401 for RE_acd1 gene expression.
  • Amplification of the “nitrilase promoter+MpAAT1 gene” fragment was performed as follows.
  • MMA-133(Sse-ProFw) (SEQ ID NO. 29) TGACCTGCAGGTGCACTCCGCTGCGACATGTATCGA MMA-131(Sse-001Rv): (SEQ ID NO. 30) ACTCTAGCCTGCAGGTCATTGACTAGTTGATCTAAGGTTGTTACA PCR Reaction Composition
  • the “nitrilase promoter+MpAAT1 gene” fragment obtained in this way was treated with restriction enzyme Sse8387I.
  • SAP treatment was performed also on pMMA401.
  • DNA fragments were purified using a Gel/PCR Purification Kit (manufactured by FAVORGEN) after performing 0.7% agarose gel electrophoresis.
  • the restriction enzyme treatment reaction conditions and ligation reaction conditions were as follows.
  • Transformation of E. coli JM109 strain was performed using a ligation reaction solution mixed in the above-mentioned composition. Plasmid was extracted from the obtained transformant. After restriction enzyme Sse8387I treatment, agarose electrophoresis was performed, and it was confirmed that a fragment of the target size is being inserted. It was confirmed as being the target plasmid from the nucleotide sequence analysis of the linkage region of the insert fragment of the obtained plasmid, and the present plasmid was named pACDAAT1.
  • a total of six plasmids for ACD and AAT co-expression of different sequences (pACDAAT2, pACDAAT3, pACDAAT4, pACDAAT6 and pACDAAT8) were prepared using the same technique as the above-mentioned technique (refer to FIG. 5 ).
  • DMA008 strain obtained in (3) of Reference Example 6 was transformed by plasmids pACDAAT1, pACDAAT2, pACDAAT3, pACDAAT4, pACDAAT6 and pACDAAT8, respectively.
  • pACDAAT1, DMA008/pACDAAT2, DMA008/pACDAAT3, DMA008/pACDAAT4, DMA008/pACDAAT6 and DMA008/pACDAAT8 was performed by the resting microorganism reaction.
  • DMA008/pLK005 was used as a control.
  • OD630 10 bacterial cell (final concentration)
  • n-butanol was used as the alcohol.
  • the DMA008 strain obtained in (3) of Reference Example 6 was transformed by plasmid pACDAAT1, respectively.
  • plasmid pACDAAT1 plasmid pACDAAT1
  • the production of methacrylic acid ester was performed by the resting microorganism reaction.
  • DMA008/pLK005 was used as a control.
  • culturing of recombinant was carried out to obtain the bacterial cell.
  • OD630 10 bacterial cell (final concentration)
  • n-butanol, isobutanol and 2-ethylhexyl alcohol were used as the alcohol.
  • Yeast-derived AAT gene expressing plasmids were prepared similarly to Example 6 (Table 12), and E. coli was transformed using these to obtain AAT expressing recombinant.
  • Cell-free extract was prepared similarly to Example 7, and the synthesis reaction of butyl methacrylate was performed with methacrylyl-CoA and n-butanol as substrate similarly to Example 8. As a result thereof, the formation of butyl methacrylate was not recognized. On the other hand, in the case of establishing acetyl-CoA and n-butanol as substrate, the formation of butyl acetate was recognized.

Abstract

Provided is a method for producing a methacrylic acid ester using a biocatalyst, said method comprising a step for treating methacrylyl-CoA with an alcohol or phenol in the presence of an alcohol acyltransferase to synthesize the methacrylic acid ester. According to this production method, a methacrylic acid ester can be efficiently produced while largely reducing energy, resource and environmental load, compared with the conventional chemical production processes.

Description

TECHNICAL FIELD
The present invention relates to a method for producing methacrylic acid ester using a biocatalyst.
BACKGROUND ART
Methacrylic acid esters are primarily used as raw material in acrylic resins, and there are many demands also as a monomer in fields such as paints, adhesives, and resin modifiers. There are a few methods as industrial manufacturing methods and, for example, the ACH (acetone cyano hydrin) method using acetone and hydrogen cyanide as raw materials, and the direct oxidation method using isobutylene and tert-butyl alcohol as raw materials have been known. These chemical production methods depend on fossil raw materials, and require great deal of energy.
In recent years, technologies for producing various chemicals from biomass as a carbon source substituting conventional fossil raw materials has been given attention from the viewpoints of prevention of global warming and environmental protection. Although the production from biomass raw material is also being expected for methacrylic acid esters, a specific production example from biomass raw materials using a biocatalyst has not been reported.
For example, methods utilizing microorganisms existing in nature to produce 2-hydroxyisobutyric acid and 3-hydroxyisobutyric acid serving precursors of methacrylic acid from a natural source such as sugar have been proposed (refer to Patent Documents 1 and 2, and Non-Patent Document 1). However, in these methods, the processes for dehydrating precursor and forming methacrylic acid still depend on chemical techniques.
In addition, although methods of forming methacrylic acid from glucose using recombinant microorganisms that do not exist in nature and are produced by introducing a plurality of enzyme genes have been proposed, these combine an already known enzyme reaction and a theoretical enzyme reaction analogized from this, and thus have not been proven (refer to Patent Documents 3 to 5). In particular, Patent Document 5 exemplifies various biocatalysts (hydrolase, wax ester synthetase, alcohol acetyltransferase) having general ester formation activity; however, it is unclear whether the exemplified biocatalysts have synthetic activity for methacrylic acid ester.
Furthermore, Patent Document 6 discloses a method for producing acrylic acid ester by causing hydrolase to function under the presence of acrylyl-CoA and alcohol. The same document suggests that production is similarly possible also for methacrylic acid esters. However, when taking account of the diversity and substrate specificity of biocatalysts, it merely illustrates that the production of a part of acrylic acid esters is possible with hydrolase, and it is unclear whether methacrylic acid esters having a different structure are similarly producible by hydrolase. Furthermore, it is completely unclear whether it is possible to produce with other types of biocatalysts having different reaction mechanisms. In addition, in the case of synthesizing esters by the hydrolase described in Patent Document 6, it is assumed that the formed ester will be decomposed by the hydrolysis activity in the first place, and thus is quite unlikely as an effective production method.
On the other hand, alcohol acetyltransferase has been known as a fruity flavor synthetase. Identifying the same enzyme genes contained in specific fruits, Patent Document 7 proposes synthesis methods of various esters that are fruit flavors. However, it has not been reported whether methacrylic acid esters are synthesizable with these enzymes, and has been completely unclear.
As stated above, although a few proposals or studies have been made, there are no examples of actually producing methacrylic acid derivatives by way of microorganisms, and thus the establishment of an effective production method has been desired.
  • [Patent Document 1] Pamphlet of PCT International Publication No. WO2007/110394
  • [Patent Document 2] Pamphlet of PCT International Publication No. WO2008/145737
  • [Patent Document 3] Pamphlet of PCT International Publication No. WO2009/135074
  • [Patent Document 4] Pamphlet of PCT International Publication No. WO2011/031897
  • [Patent Document 5] Pamphlet of PCT International Publication No. WO2012/135789
  • [Patent Document 6] Pamphlet of PCT International Publication No. WO2007/039415
  • [Patent Document 7] Pamphlet of PCT International Publication No. WO2000/32789
  • [Patent Document 8] Japanese Unexamined Patent Application, Publication No. 2011-200133
  • [Patent Document 9] Japanese Unexamined Patent Application, Publication No. H05-64589
  • [Patent Document 10] Japanese Unexamined Patent Application, Publication No. H10-337185
  • [Patent Document 11] Japanese Unexamined Patent Application, Publication No. H10-24867
  • [Non-Patent Document 1] Green Chemistry, 2012, 14, 1942-1948
  • [Non-Patent Document 2] Methods in Enzymology, 2000, 324, 73-79
  • [Non-Patent Document 3] Botanical Journal of the Linnean Society, 2009, 161, 105-121
  • [Non-Patent Document 4] Microbiology, 1999, 145, 2323-2334
DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention
The present invention has an object of providing a method for producing methacrylic acid ester by way of a biocatalyst.
Means for Solving the Problems
It has been found that alcohol acyltransferase has activity for synthesizing methacrylic acid esters, thereby arriving at completion of the present invention. More specifically, the present invention is as follows.
According to a first aspect of the invention, a method for producing methacrylic acid ester includes a step of synthesizing methacrylic acid ester by causing an alcohol or phenol to act on methacrylyl-CoA under the presence of an alcohol acyltransferase.
According to a second aspect of the invention, in the method for producing methacrylic acid ester as described in the first aspect, the methacrylic acid ester is accumulated in at least 0.001 mM.
According to a third aspect of the invention, the method for producing methacrylic acid ester as described in the first or second aspect further includes a step of producing methacrylyl-CoA from isobutyryl-CoA or 3-hydroxyisobutyryl-CoA.
According to a fourth aspect of the invention, in the method for producing methacrylic acid ester as described in the third aspect, the isobutyryl-CoA is produced from 2-oxoisovaleric acid.
According to a fifth aspect of the invention, in the method for producing methacrylic acid ester as described in any one of the first to fourth aspects, the alcohol acyltransferase is of plant origin.
According to a sixth aspect of the invention, in the method for producing methacrylic acid ester as described in the fifth aspect, the plant belongs to any order selected from the group consisting of Zingiberales, Rosales, Ericales, Cucurbitales, Brassicales and Laurales.
According to a seventh aspect of the invention, in the method for producing methacrylic acid ester as described in the fifth aspect, the plant belongs to any family selected from the group consisting of Musaceae, Rosaceae, Ericaceae, Actinidiaceae, Cucurbitaceae, Caricaceae and Lauraceae.
According to an eighth aspect of the invention, in the method for producing methacrylic acid ester as described in the fifth aspect, the plant belongs to any genus selected from the group consisting of Musa, Fragaria, Malus, Prunus, Pyrus, Vaccinium, Actinidia, Cucumis, Carica and Persea.
According to a ninth aspect of the invention, in the method for producing methacrylic acid ester as described in the fifth aspect, the plant is any genus selected from Musa, Malus, Prunus, Pyrus, Vaccinium, Actinidia, Cucumis, Carica and Persea.
According to a tenth aspect of the invention, in the method for producing methacrylic acid ester as described in the fifth aspect, the plant is any genus selected from Musa, Malus, Pyrus, Actinidia, Cucumis, Carica and Persea.
According to an eleventh aspect of the invention, in the method for producing methacrylic acid ester as described in the fifth aspect, the plant is any one selected from the group consisting of banana, strawberry, apple, Prunus mume, Pyrus communis, blueberry, kiwi, melon, papaya and avocado.
According to a twelfth aspect of the invention, in the method for producing methacrylic acid ester as described in the fifth aspect, the plant is any one selected from the group consisting of banana, apple, Prunus mume, Pyrus communis, blueberry, kiwi, melon, papaya and avocado.
According to a thirteenth aspect of the invention, in the method for producing methacrylic acid ester as described in the fifth aspect, the plant is any one selected from the group consisting of banana, apple, Pyrus communis, kiwi, melon, papaya and avocado.
According to a fourteenth aspect of the invention, the method for producing methacrylic acid ester as described in any of the first to thirteenth aspects uses a genetically modified microorganism that has been gene transferred so as to express alcohol acyltransferase.
In addition, the present invention is as follows in another aspect.
According to a fifteenth aspect of the invention, a method for producing methacrylic acid ester produces the methacrylic acid ester using a microorganism belonging to Rhodococcus genus.
According to a sixteenth aspect of the invention, the method for producing methacrylic acid ester as described in the fifteenth aspect uses a microorganism belonging to the Rhodococcus genus having 16SrDNA that includes a nucleotide sequence having at least 95% identity to the nucleotide sequence of 16SrDNA shown in SEQ ID NO. 31.
According to a seventeenth aspect of the invention, in the method for producing methacrylic acid ester as described in the fifteenth or sixteenth aspect, the microorganism belonging to Rhodococcus genus is Rhodococcus erythropolis.
According to an eighteenth aspect of the invention, the method for producing methacrylic acid ester as described in the fifteenth or sixteenth aspect uses a derivative strain of the microorganism as the microorganism belonging to Rhodococcus genus.
According to a nineteenth aspect of the invention, in the method for producing methacrylic acid ester as described in the eighteenth aspect, the microorganism belonging to Rhodococcus genus is Rhodococcus erythropolis PR-4 strain or a derivative strain thereof.
According to a twentieth aspect of the invention, in the method for producing methacrylic acid ester as described in the eighteenth aspect, the derivative strain is a genetically modified strain having a modification of at least one of (a) or (b) shown below.
(a) Modification by introduction of branched ketoacid dehydrogenase gene and/or acyl-CoA dehydrogenase gene
(b) Modification of deleting or inactivating enoyl-CoA hydratase gene, 3-hydroxyisobutyryl-CoA hydratase gene and/or 3-hydroxyisobutyric acid dehydrogenase gene.
According to a twenty-first aspect of the invention, in the method for producing methacrylic acid ester as described in the nineteenth or twentieth aspect, the derivative strain has a plasmid for alcohol acyltransferase and/or acyl-CoA dehydrogenase expression.
Effects of the Invention
By way of the present invention, the production of methacrylic acid ester by way of a biocatalyst becomes possible. By combining the production method of the present invention with in vivo metabolism, fermentative production of methacrylic acid ester can also be achieved. As a result thereof, the energy, resources and load on the environment can be remarkably reduced compared to a conventional chemical production process, and it becomes possible to efficiently produce methacrylic acid ester.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a view showing the production steps from 3-hydroxyisobutyryl-CoA to methacrylic acid ester;
FIG. 2 is a view showing the production steps from 2-oxoisovaleric acid to methacrylic acid ester;
FIG. 3 is a view showing the structure of a plasmid for LigD homolog gene deletion;
FIG. 4 is a view illustrating a preparation method for plasmid for gene deletion using the In Fusion method; and
FIG. 5 is a view showing the structures of plasmids for ACD-AAT co-expression.
 EMBODIMENTS FOR CARRYING OUT THE INVENTION
Hereinafter, preferred modes for carrying out the present invention will be explained while referencing the drawings. It should be noted that the embodiments explained in the following are arrived at by expressing examples of representative embodiments of the present invention, and the scope of the present invention is not to be narrowly interpreted therefrom.
1. Production Method of Methacrylic Acid Ester from Alcohol Acyltransferase
Methacrylic Acid Ester
In the present invention, methacrylic acid ester is a compound expressed by Formula 1. In Formula 1, R represents a linear or branched C1-20 hydrocarbon group. The hydrocarbon group may be of saturated or unsaturated non-cyclic type, or may be of saturated or unsaturated cyclic type. It is preferably a linear or branched C1-10 unsubstituted alkyl group, aralkyl group or aryl group. It is more preferably a C1-8 alkyl group such as a methyl group, ethyl group, n-propyl group, isopropyl group, n-butyl group, isobutyl group, sec-butyl group, tert-butyl group, n-pentyl group, isopentyl group, tert-pentyl group, n-hexyl group, isohexyl group, 2-hexyl group, dimethylbutyl group, ethylbutyl group, heptyl group, octyl group, 2-ethylhexyl group; a benzyl group or a phenyl group.
CH2═C(CH3)COO—R  (Formula 1)
“Methacrylic acid” (IUPAC name: 2-methyl-2-propenoic acid) indicates a compound having the formula below, and also includes any salts or ionized forms thereof. As salts of methacrylic acid, for example, sodium salts, potassium salts, calcium salts, magnesium salts, etc. can be exemplified.
CH2═C(CH3)COOH
Methacrylyl-CoA
In the present invention, methacrylyl-CoA is a compound expressed by the structural formula below. Methacrylyl-CoA is known as a metabolic intermediate of valine within organisms. The methacrylyl-CoA used in the present invention can be that produced by a known or novel method. As the synthesis method thereof, the method of organochemically synthesizing coenzyme A with methacrylic anhydride (Methods in Enzymology, 324, 73-79 (2000)) or a synthesis method using an enzyme reaction are known.
Figure US10851392-20201201-C00001
In the present invention, among these, methacrylyl-CoA (refer to FIG. 2) transformed by the action of acyl-CoA dehydrogenase (EC 1.3.99.3) (hereinafter referred to as ACD) with isobutyryl-CoA as a raw material or methacrylyl-CoA (refer to FIG. 1) transformed by action of enoyl-CoA hydratase (EC 4.2.1.17) (hereinafter referred to as ECH) from 3-hydroxyisobutyryl-CoA can be favorably used. In other words, the method of the present invention preferably further includes a step of producing methacrylyl-CoA from isobutyryl-CoA or 3-hydroxyisobutyryl-CoA. From the continuous reaction by enzyme, together with being connecting to a yield improvement as well as foreign matter suppression, the direct synthesis of methacrylic acid ester becomes possible without going through methacrylic acid having high toxicity to organisms, or forming byproducts. According to the method, it is possible to achieve production of methacrylic acid ester by an in vivo continuous reaction (metabolic fermentation) with low environmental burden.
For the isobutyryl-CoA used in the present invention, one produced from 2-oxoisovaleric acid can be used (refer to FIG. 2). In other words, the method of the present invention may further include a step of producing isobutyryl-CoA from 2-oxoisovaleric acid.
Alcohols and Phenols
The alcohols or phenols serving as raw materials in the production of the methacrylic acid ester in the present invention are compounds expressed by formula 2 below. The structure of the alcohol or phenols corresponds to methacrylic acid ester; therefore, the structure thereof is defined the same as R in Formula 1, and represents a linear or branched C1-20 hydrocarbon group. The hydrocarbon group may be of saturated or unsaturated non-cyclic type, or may be of saturated or unsaturated cyclic type. It is preferably a linear or branched C1-10 unsubstituted alcohol, aralkyl alcohol or phenol, and particularly preferably a C1-8 alkyl alcohol such as methanol, ethanol, n-propanol, isopropanol, n-butanol, isobutanol, sec-butanol, tert-butanol, n-pentylalcohol, isopentyl alcohol, tert-pentyl alcohol, n-hexyl alcohol, isohexyl alcohol, 2-hexyl alcohol, dimethylbutyl alcohol, ethylbutyl alcohol, heptyl alcohol, octyl alcohol, 2-ethylhexyl alcohol; a benzyl alcohol or a phenol.
R—OH  (Formula 2)
Alcohol Acyltransferase
The alcohol acyltransferase of the present invention (hereinafter referred to as AAT) is an enzyme having a catalytic action for synthesizing ester by causing the acyl group of acyl-CoA to transfer to the alcohol or phenol. AAT is considered to participate in the formation of esters in various fruits. AAT is known to be present in plants such as Zingiberales (banana), Rosales (strawberry, apple, pear, peach), Cucurbitales (melon), Ericales (kiwi), Lamiales (olive), Solanales (tomato), and Sapindales (lemon, mango).
The AAT used in the present invention is not particularly limited so long as being a catalyst of biological origin having a capacity to produce methacrylic acid ester with methacrylyl-CoA and alcohol or phenol as raw materials, and the kind and origin thereof are not of concern. One of plant origin is preferable as the enzyme source, and thereamong, one categorized as an angiosperm is preferable.
The AAT suited to the present invention can be easily selected from the plants by the following method. An appropriate part of the tissue is acquired by cutting as necessary. A solution containing methacrylyl-CoA and an alcohol or phenol represented by Formula 2 are added to this cut part, shaken, and allowed to react for a certain time. It is possible to confirm the synthetic activity by confirming the presence of methacrylic acid ester in this reaction solution by GC (gas chromatography). More specifically, for example, the sarcocarp or pericarp is cut, a solution containing 1 to 10 mM methacrylyl-CoA, 0.35 KCl and 5 to 50 times molar quantity of n-butanol is added thereto, and shaken for 1 to 10 hours at 30° C. After reaction completion, an AAT applicable to the present invention can be selected by confirming the presence of methacrylic acid ester by way of GC.
The enzyme source of AAT suited to the present invention, for example, is one belonging to any order selected from the group consisting of Zingiberales, Rosales, Ericales, Cucurbitales, Brassicales, Laurales, Poales, Arecales, Asparagales, Saxifragales, Caryophyllales, Vitales, Malpighiales, Oxalidales, Fabales, Sapindales, Malvales, Myrtales, Ranunculales, Solanales, Lamiales, Gentianales and Asterales. Thereamong, it is preferably one belonging to any order selected from the group consisting of Zingiberales, Rosales, Ericales, Cucurbitales, Brassicales and Laurales.
Plants of Musaceae and Zingiberaceaeare are preferable as those belonging to the order Zingiberales; plants of Rosaceae and Moraceae are preferable as those belonging to the order Rosales; plants of Ericaceae, Actinidiaceae, Ebenaceae and Theaceae are preferable as those belonging to the order Ericales; plants of Cucurbitaceae are preferable as those belonging to the order Cucurbitales; plants of Caricaceae and Brassicaceae are preferable as those belonging to the order Brassicales; plants of Lauraceae are preferable as those belonging to the order Laurales; plants of Bromeliaceae and Poaceae are preferable as those belonging to the order Poales; plants of Arecaceae are preferable as those belonging to the order Arecales; plants of Orchidaceae and Iridaceae are preferable as those belonging to the order Asparagales; plants of Grossulariaceae are preferable as those belonging to the order Saxifragales; plants of Caryophyllaceae are preferable as those belonging to the order Caryophyllales; plants of Vitaceae are preferable as those belonging to the order Vitales; plants of Malpighiaceae, Passifloraceae, Euphorbiaceae and Salicaceae are preferable as those belonging to the order Malpighiales; plants of Oxalidaceae are preferable as those belonging to the order Oxalidales; plants of Fabaceae are preferable as those belonging to the order Fabales; plants of Rutaceae, Sapindaceae and Anacardiaceae are preferable as those belonging to the order Sapindales; plants of Malvaceaeare are preferable as those belonging to the order Malvales; plants of Lythraceae, Onagraceae and Myrtaceae are preferable as those belonging to the order Myrtales; plants of Ranunculaceae and Papaveraceae are preferable as those belonging to the order Ranunculales; plants of Solanaceae are preferable as those belonging to the order Solanales; plants of Oleaceae, Verbenaceae and Lamiaceae are preferable as those belonging to the order Lamiales; plants of Apocynaceae are preferable as those belonging to the order Gentianales; and plants of Asteraceae are preferable as those belonging to the order Asterales. A related species of the above-mentioned plants can also be employed. Thereamong, it is more preferably a plant belonging to Musacea, Rosaceae, Ericeae, Actinidiaceae, Cucurbitaceae, Caricaceae or Lauraceae.
More specifically, plants of Musa are preferable as those belonging to the family Musaceae; plants of Zingiber are preferable as those belonging to the family Zingiberaceae; plants of Fragaria, Malus, Prunus, Pyrus, Eriobotrya, Chaenomeles, Rubus and Rosa are preferable as those belonging to the family Rosaceae; plants of Ficus are preferable as those belonging to the family Moraceae; plants of Vaccinium are preferable as those belonging to the family Ericaceae; plants of Actinidia are preferable as those belonging to the family Actinidiaceae; plants of Diospyros are preferable as those belonging to the family Ebenaceae; plants of Camellia are preferable as those belonging to the family Theaceae; plants of Cucumis and Citrullus are preferable as those belonging to the family Cucurbitaceae; plants of Carica and Vasconcellea are preferable as those belonging to the family Caricaceae; plants of Arabidopsis are preferable as those belonging to the family Brassicaceae; plants of Persea are preferable as those belonging to the family Lauraceae; plants of Ananas are preferable as those belonging to the family Bromeliaceae; plants of Oryza, Triticum, Hordeum, Zea, Sorghum and Brachypodium are preferable as those belonging to the family Poaceae; plants of Cocus are preferable as those belonging to the family Arecaceae; plants of Vanda are preferable as those belonging to the family Orchidaceae; plants of Iris are preferable as those belonging to the family Iridaceae; plants of Ribes are preferable as those belonging to the family Grossulariaceae; plants of Gypsophila are preferable as those belonging to the family Caryophyllaceae; plants of Vitis are preferable as those belonging to the family Vitaceae; plants of Malpighia are preferable as those belonging to the family Malpighiaceae; plants of Passiflora are preferable as those belonging to the family Passifloraceae; plants of Ricinus are preferable as those belonging to the family Euphorbiaceae; plants of Populusare preferable as those belonging to the family Salicaceae; plants of Averrhoaare preferable as those belonging to the family Oxalidaceae; plants of Medicago, Lupinus, Glycine and Clitoria are preferable as those belonging to the family Fabaceae; plants of Citrus and Aegle are preferable as those belonging to the family Rutaceae; plants of Litchi are preferable as those belonging to the family Sapindaceae; plants of Mangifera are preferable as those belonging to the family Anacardiaceae; plants of Durioand Theobroma are preferable as those belonging to the family Malvaceae; plants of Punica are preferable as those belonging to the family Lythraceae; plants of Clarkia are preferable as those belonging to the family Onagraceae; plants of Psidium are preferable as those belonging to the family Myrtaceae; plants of Actaea are preferable as those belonging to the family Ranunculaceae; plants of Papaver are preferable as those belonging to the family Papaveraceae; plants of Solanum, Capsicum, Nicotiana and Petunia are preferable as those belonging to the family Solanaceae; plants of Olea are preferable as those belonging to the family Oleaceae; plants of Glandularia are preferable as those belonging to the family Verbenaceae; plants of Salvia are preferable as those belonging to the family Lamiaceae; plants of Rauvolfia and Catharanthus are preferable as those belonging to the family Apocynaceae; and plants of Chamaemelum are preferable as those belonging to the family Asteraceae. Thereamong, plants belonging to Musa, Fragaria, Malus, PRunus, Pyrus, Vaccinium, Actinidia, Cucumis, Carica or Persea are more preferable. Furthermore, thereamong, plants belonging to Musa, Malus, Pyrus, Actinidia, Cucumis, Carica or Persea are particularly preferable.
Furthermore, more specifically, plants of Musaxparadisiaca, Musabasjoo, Musacoccinea and Musaacuminata are particularly preferable as those belonging to the genus Musa; plants of Zingiberofficinale are particularly preferable as those belonging to the genus Zingiber; plants of Fragariaxananassa, Fragariavirginiana, Fragariachiloensis and Fragariavesca are particularly preferable as those belonging to the genus Fragaria; plants of Maluspumila, Malusdomestica, Malusbaccata, Malushalliana, Malusfloribunda and Malusprunifolia are particularly preferable as those belonging to the genus Malus; plants of Prunusmume, Prunusavium, Prunuspersica, Prunusarmeniaca, Prunusdulcis, Prunussalicina and Prunusdomestica are particularly preferable as those belonging to the genus Prunus; plants of Pyruscommunis, Pyruspyrifolia, Pyruscalleryana and Pyruspyraster are particularly preferable as those belonging to the genus Pyrus; plants of Eriobotryajaponica are particularly preferable as those belonging to the genus Eriobotrya; plants of Chaenomelessinensis are particularly preferable as those belonging to the genus Chaenomeles; plants of Rubusidaeus and Rubusfruticosus are particularly preferable as those belonging to the genus Rubus; plants of Rosarugosa are particularly preferable as those belonging to the genus Rosa; plants of Ficuscarica are particularly preferable as those belonging to the genus Ficus; plants of Vacciniumcorymbosum, Vacciniumangustifolium, Vacciniummyrtillus, Vacciniumvitis-idaea and Vacciniumoxycoccos are particularly preferable as those belonging to the genus Vaccinium; plants of Actinidiachinensis, Actinidiadeliciosa, Actinidiaarguta, Actinidiarufa and Actinidiapolygama are particularly preferable as those belonging to the genus Actinidia; plants of Diospyroskaki are particularly preferable as those belonging to the genus Diospyros; plants of Camelliasinensis are particularly preferable as those belonging to the genus Camellia; plants of Cucumissativus, Cucumismelo, Cucumisanguria and Cucumismetulifer are particularly preferable as those belonging to the genus Cucumis; plants of Citrulluslanatus are particularly preferable as those belonging to the genus Citrullus; plants of Caricapapaya are particularly preferable as those belonging to the genus Caricaceae; plants of Vasconcelleacundinamarcensis are particularly preferable as those belonging to the genus Vasconcellea; plants of Arabidopsisthaliana and Arabidopsislyrata are particularly preferable as those belonging to the genus Arabidopsis; plants of Perseaamericana are particularly preferable as those belonging to the genus Persea; plants of Ananascomosus are particularly preferable as those belonging to the genus Ananas; plants of Oryzasativa are particularly preferable as those belonging to the genus Oryza; plants of Triticumaestivum are particularly preferable as those belonging to the genus Triticum; plants of Hordeumvulgare are particularly preferable as those belonging to the genus Hordeum; plants of Zeamays are particularly preferable as those belonging to the genus Zea; plants of Sorghumbicolor are particularly preferable as those belonging to the genus Sorghum; plants of Brachypodiumdistachyon are particularly preferable as those belonging to the genus Brachypodium; plants of Cocosnucifera are particularly preferable as those belonging to the genus Cocos; plants of Vandahybridcultivar are particularly preferable as those belonging to the genus Vanda; plants of Irisxhollandica are particularly preferable as those belonging to the genus Iris; plants of Ribesnigrum are particularly preferable as those belonging to the genus Ribes; plants of Gypsophilapaniculata and Gypsophilaelegans are particularly preferable as those belonging to the genus Gypsophila; plants of Vitisvinifera and Vitislabrusca are particularly preferable as those belonging to the genus Vitis; plants of Malpighiaglabra are particularly preferable as those belonging to the genus Malpighia; plants of Passifloraedulis are particularly preferable as those belonging to the genus Passiflora; plants of Ricinuscommunis are particularly preferable as those belonging to the genus Ricinus; plants of Populustrichocarpa are particularly preferable as those belonging to the genus Populus; plants of Averrhoacarambola are particularly preferable as those belonging to the genus Averrhoa; plants of Medicagotruncatula are particularly preferable as those belonging to the genus Medicago; plants of Lupinusalbus are particularly preferable as those belonging to the genus Lupinus; plants of Glycinemax are particularly preferable as those belonging to the genus Glycine; plants of Clitoriaternatea are particularly preferable as those belonging to the genus Clitoria; plants of Citruslimon, Citrussudachi, Citrussphaerocarpa, Citrusxparadisi, Citrusjunos, Citrusaurantifolia, Citrusunshiu and Citrussinensis are particularly preferable as those belonging to the genus Citrus; plants of Aeglemarmelos are particularly preferable as those belonging to the genus Aegle; plants of Litchichinensi are particularly preferable as those belonging to the genus Litchi; plants of Mangiferaindica are particularly preferable as those belonging to the genus Mangifera; plants of Duriozibethinus are particularly preferable as those belonging to the genus Durio; plants of Theobromacacao are particularly preferable as those belonging to the genus Theobroma; plants of Punicagranatum are particularly preferable as those belonging to the genus Punica; plants of Clarkiabreweri and Clarkiaconcinna are particularly preferable as those belonging to the genus Clarkia; plants of Psidiumguajava are particularly preferable as those belonging to the genus Psidium; plants of Actaearacemosa are particularly preferable as those belonging to the genus Actaea; plants of Papaversomniferum, Papaverorientale and Papaverbracteatum are particularly preferable as those belonging to the genus Papaver; plants of Solanumlycopersicum are particularly preferable as those belonging to the genus Solanum; plants of Capsicumannuum and Capsicumchinense are particularly preferable as those belonging to the genus Capsicum; plants of Nicotianatabacum and Nicotianaattenuata are particularly preferable as those belonging to the genus Nicotiana; plants of Petuniaxhybrida are particularly preferable as those belonging to the genus Petunia; plants of Oleaeuropaea are particularly preferable as those belonging to the genus Olea; plants of Glandulariaxhybrida are particularly preferable as those belonging to the genus Glandularia; plants of Salviasplendens are particularly preferable as those belonging to the genus Salvia; plants of Rauvolfiaserpentina are particularly preferable as those belonging to the genus Rauvolfia; plants of Catharanthusroseus are particularly preferable as those belonging to the genus Catharanthus; and plants of Chamaemelumnobile are particularly preferable as those belonging to the genus Chamaemelum. Thereamong, banana, strawberry, apple, Japanese apricot, European pear, blueberry, kiwi, melon, papaya or avocado is more preferable. Furthermore, thereamong, banana, apple, European pear, kiwi, melon, papaya or avocado is particularly preferable.
It should be noted that, in the case of performing the synthetic reaction using a plant as is as the enzyme source, in particular, it is more preferable to use plants belonging to Malus, Carica and Persea, when defining a C1-2 alcohol as the substrate. This is due to having higher generation efficiency than plants belonging to another genus.
In the present invention, the classifications of plant are defined following Botanical Journal of the Linnean Society, 2009, 161, 105121.
In the present invention, upon supplying AAT for reaction, mode of use is not particularly limited so long as exhibiting the above-mentioned catalytic activity, and it is possible to use the biological tissue or processed product thereof as is. As such biological tissue, the entire planta, plant organs (e.g., fruit, leaves, petals, stem, seed, etc.), or plant tissue (e.g., fruit skin, sarcocarp, etc.) can be used. As the processed product thereof, the crude enzyme liquid from extracting AAT from these biological tissues, purified enzyme, or the like can be exemplified.
AAT Activity Expression Recombinant Microorganism
Furthermore, upon supplying AAT for reaction, the gene for the AAT is isolated, for example, introduced to a general host vector system, and the microorganism transformed by this vector system can be used. As the host, as for bacteria, E. coli, Rhodococcus, Pseudomonas, Corynebacterium, Bacillus, Streptococcus, Streptomyces, etc. can be exemplified; as for yeast, Saccharomyces, Candida, Shizosaccharomyces and Pichia; and as for filamentous fungus, Aspergillus, etc. can be exemplified. Among these, it is particularly easy to use bacteria, and is also preferable in efficiency.
Several AAT genes have been published (for example, refer to Patent Document 7). A DNA probe is prepared based on this publication, and for example, a primer used in PCR is prepared, and this gene can be isolated by performing PCR. In addition, it is also possible to completely synthesize the nucleotide sequence of AAT gene by a common method. It can be similarly confirmed by the method whether these AAT for which genetic information is known have synthetic activity for methacrylic acid ester. On the other hand, for AAT having unclear genetic information, AAT can be purified, and genetic information can be obtained by a genetic engineering method on the basis of proteins thereof.
As a preferred AAT gene in the present invention, it is not particularly limited so long as the translated product thereof has a capability of producing methacrylic acid ester, and is appropriately selected from among the AAT enzymes sources. Particularly preferably, AAT apple-derived AAT gene (SEQ ID NO: 2), strawberry-derived AAT gene (SEQ ID NO: 4) and strawberry-derived AAT gene (SEQ ID NO: 6) can be exemplified.
It should be noted that genes coding proteins having activity to produce methacrylic acid ester from methacrylyl-CoA and alcohol including an amino acid sequence in which one or a plurality of amino acids have been substituted, deleted or added to a wild-type amino acid sequence are also included in the AAT genes of the present invention.
Herein, the term “plurality” refers to 1 to 40, preferably 1 to 20, and more preferably no more than 10. In order to introduce mutation to the gene, it is possible to use a kit for mutation introduction using a site-directed mutagenesis method, for example, QuikChange™ Site-Directed Mutagenesis Kit (Stratagene), GeneTailor™ Site-Directed Mutagenesis System (Invitrogen), TaKaRa Site-Directed Mutagenesis System (Mutan-K, Mutan-Super Express Km, etc.: Takara Bio), etc., by a known method such as the Kunkel method or Gapped duplex method. Alternatively, the entire gene having a sequence including mutation may be artificially synthesized.
In the present invention, confirmation of the nucleotide sequence of DNA can be performed by sequence determination by a common method. For example, based on Sanger's method, it is possible to confirm the sequence using an appropriate DNA sequencer.
In addition, in the AAT gene of the present invention, genes coding proteins having activity to produce methacrylic acid ester from methacrylyl-CoA and alcohol expressing at least 90% identity with the protein consisting of the wild-type amino acid sequence, preferably 95%, more preferably 99.5%, and even more preferably 99.9%, are also included.
Furthermore, in the AAT gene of the present invention, genes hybridizing under stringent conditions to a polynucleotide having the complementary nucleotide sequence to the wild-type nucleotide sequence, and coding protein having activity to produce methacrylic acid ester from methacrylyl-CoA and alcohol are also included. As the stringent conditions, for example, it is possible to exemplify conditions of perform hybridization by maintaining a nylon membrane fixing the DNA at the same temperature while probing at 65° C. for 20 hours in a solution containing 6×SSC (1×SSC is prepared by dissolving 8.76 g of sodium chloride and 4.41 g of sodium citrate in 1 liter of water), 1% SDS, 100 μg/ml salmon sperm DNA, 0.1% bovine serum albumin, 0.1% polyvinylpyrrolidone and 0.1% ficoll. For one skilled in the art, it is possible to take account of other terms and conditions such as probe concentration, length of probe, and reaction time in addition to such conditions as salt concentration, temperature of buffer, etc. so as to set the conditions of hybridization. As drying conditions after hybridization, for example, “2×SSC, 0.1% SDS, 42° C.” and “1×SSC, 0.1% SDS, 37° C.”, and as more stringent conditions, for example, conditions such as “1×SSC, 0.1% SDS, 65° C.” and “0.5×SSC, 0.1% SDS, 50° C.” can be exemplified.
Regarding the detailed sequence of the hybridization method, it is possible to refer to Molecular Cloning, A Laboratory Manual 2nd ed. (Cold Spring Harbor Laboratory Press (1989)), Current Protocols in Molecular Biology (John Wiley & Sons (1987-1997)), or the like.
Furthermore, in the AAT gene of the present invention, when calculating using the wild-type nucleotide sequence, BLAST, etc. (e.g., default, i.e. initial setting, parameters), genes coding protein having activity to produce methacrylic acid ester from methacrylyl-CoA and alcohol consisting of a nucleotide sequence having identity of at least 80%, more preferably at least 90%, and more preferably at least 95% are also included. In addition, the codons of the above-mentioned AAT genes may be changed according to the codon frequency of use in the microorganism host used in genetic transformation.
Herein, “identity” of the sequence, when the case of a nucleotide sequence, is arrived at by aligning both nucleotide sequences so that the bases of the two nucleotide sequences to be compared match as much as possible, and then expressing a value arrived at by subtracting the number of matching bases from the total number of bases as a percentage. Upon the above-mentioned alignment, appropriate gaps are inserted into one or both of the two sequences compared as necessary. Such an alignment of sequences can be performed using a known program such as BLAST, FASTA, and CLUSTAL, for example. In the case of gaps being inserted, the above-mentioned total number of bases becomes the number of bases arrived at by counting one gap as one base. In the case of the total number of bases arrived at by counting in this way differing between the two sequences compared, the identity (%) is calculated by subtracting the matching number of bases from the total number of bases in the longer sequence. This similarly applies also for the identity of amino acid sequences.
In the methacrylic acid ester synthesis reaction, it is possible to use the broth obtained by culturing these recombinant microorganisms as is, or use the bacterial cell obtained by a harvesting operation such as centrifugation from this broth, a processed product thereof, or the like. As the bacterial cell processed product, a bacterial cell treated with acetone, toluene or the like, freeze-dried bacterial cells, disrupted bacterial cells, or noncellular extract from disrupted bacterial cells, crude enzyme extracted from these enzymes or purified enzyme, etc. can be exemplified.
Methacrylic acid ester can also be synthesized with isobutyryl-CoA or 3-hydroxyisobutyryl-CoA as a raw material by simultaneously introducing ACD gene or ECH gene with AAT gene (refer to FIG. 1 and FIG. 2). Furthermore, by combining and introducing 2-oxoisovaleric acid dehydrogenase gene (hereinafter referred to as BCKAD), it is also possible to synthesize methacrylic acid from 2-oxoisovaleric acid.
Although there is no particular limitation in the origins of ACD, ECH and BCKAD in the present invention, the microorganisms listed below can be exemplified.
It is a microorganism belonging to the genus Magnetospirillum, Rhodospirillum, Azospirillum, Tistrella, Acidiphilium, Rhodobacter, Paracoccus, Ruegeria, Jannaschia, Roseobacter, Dinoroseobacter, Pseudovibrio, Phaeobacter, Octadecabacter, Hyphomonas, Maricaulis, Hirschia, Sphingomonas, Novosphingobium, Sphingopyxis, Sphingobium, Erythrobacter, Brevundimonas, Caulobacter, Phenylobacterium, Asticcacaulis, Agrobacterium, Rhizobium, Sinorhizobium, Xanthobacter, Azorhizobium, Brucella, Ochrobactrum, Mesorhizobium, Chelativorans, Aurantimonas, Bradyrhizobium, Agromonas, Rhodopseudomonas, Nitrobacter, Methylobacterium, Rhodomicrobium, Pelagibacterium, Parvibaculum, Methylocystis, Parvularcula, Burkholderia, Ralstonia, Cupriavidus, Polynucleobacter, Achromobacter, Bordetella, Taylorella, Pusillimonas, Comamonas, Alicycliphilus, Delftia, Ramlibacter, Rhodoferax, Variovorax, Polaromonas, Acidovorax, Verminephrobacter, Herminiimonas, Herbaspirillum, Collimonas, Chromobacterium, Laribacter, Pseudogulbenkiania, Nitrosomonas, Nitrosospira, Aromatoleum, Azoarcus, Dechloromonas, Thauera, Azospira (Dechlorosoma), Rheinheimera, Nitrosococcus, Halorhodospira, Xanthomonas, Stenotrophomonas, Pseudoxanthomonas, Rhodanobacter, Francisella, Cycloclasticus, Oceanospirillum, Hahella, Halomonas, Alcanivorax, Kangiella, Pseudomonas, Azotobacter, Acinetobacter, Psychrobacter, Alishewanella, Alteromonas, Glaciecola, Marinobacter, Marinobacterium, Saccharophagus, Shewanella, Ferrimonas, Idiomarina, Colwellia, Pseudoalteromonas, Listonella, Vibrio, Photobacterium, Aeromonas, Oceanimonas, Salinisphaera, Legionella, Coxiella, Desulfococcus, Desulfobacterium, Desulfatibacillum, Desulfobulbus, Desulfarculus, Geobacter, Syntrophobacter, Syntrophus, Desulfomonile, Bdellovibrio, Bacteriovorax, Stigmatella, Myxococcus, Anaeromyxobacter, Sorangium, Haliangium, Acidobacterium, Granulicella, Ilumatobacter, Streptosporangium, Nocardiopsis, Thermobifida, Thermomonospora, Pseudonocardia, Amycolatopsis, Saccharomonospora, Saccharopolyspora, Thermobispora, Actinosynnema, Micromonospora, Salinispora, Verrucosispora, Nocardioides, Kribbella, Corynebacterium, Nocardia, Rhodococcus, Gordonia, Dietzia, Mycobacterium, Amycolicicoccus, Tsukamurella, Segniliparus, Microbacterium, Micrococcus, Arthrobacter, Citricoccus, Renibacterium, Kocuria, Kytococcus, Cellulomonas, Intrasporangium, Serinicoccus, Frankia, Acidothermus, Nakamurella, Geodermatophilus, Stackebrandtia, Streptomyces, Catenulispora, Rubrobacter, Conexibacter, Bacillus, Geobacillus, Oceanobacillus, Lysinibacillus, Halobacillus, Alicyclobacillus, Kyrpidia, Paenibacillus, Lactobacillus, Carnobacterium, Clostridium, Alkaliphilus, Syntrophomonas, Syntrophothermus, Eubacterium, Desulfitobacterium, Desulfotomaculum, Pelotomaculum, Butyrivibrio, Roseburia, Oscillibacter, Thermoanaerobacter, Carboxydothermus, Natranaerobius, Sphingobacterium, Pedobacter, Haliscomenobacter, Porphyromonas, Odoribacter, Spirosoma, Runella, Maribacter, Deinococcus, Thermus, Meiothermus, Oceanithermus, Marinithermus, Gemmatimonas, Fusobacterium, Ilyobacter, Roseiflexus, Herpetosiphon, Thermomicrobium, Thermotoga, Thermosipho, Fervidobacterium, Deferribacter, Calditerrivibrio, Flexistipes, Metallosphaera, Aeropyrum, Pyrobaculum, Caldivirga, Vulcanisaeta, Acidilobus, Haloarcula, Haloquadratum, Natronomonas, Halorubrum, Haloterrigena, Natrialba, Halalkalicoccus, Halogeometricum, Thermoplasma, Picrophilus, Ferroplasma, Archaeoglobus, Ferroglobus, Polymorphum, Micavibrio, Simiduia, Leptothrix, Thiomonas, Rubrivivax, Methylibium, Exiguobacterium and Anaerococcus.
Furthermore, Magnetospirillum magneticum is particularly preferable as the microorganism classified as Magnetospirillum; Rhodospirillum rubrum, Rhodospirillum centenum and Rhodospirillum photometricum are particularly preferable as the microorganism classified as Rhodospirillum; Azospirillum lipoferum and Azospirillum brasilense are particularly preferable as the microorganism classified as Azospirillum; Tistrella mobilis is particularly preferable as the microorganism classified as Tistrella; Acidiphilium cryptum and Acidiphilium multivorum are particularly preferable as the microorganism classified as Acidiphilium; Rhodobacter sphaeroides and Rhodobacter capsulatus are particularly preferable as the microorganism classified as Rhodobacter; Paracoccus denitrificans and Paracoccus aminophilus are particularly preferable as the microorganism classified as Paracoccus; Ruegeria pomeroyi is particularly preferable as the microorganism classified as Ruegeria; Roseobacter denitrificans and Roseobacter litoralis are particularly preferable as the microorganism classified as Roseobacter; Dinoroseobacter shibae is particularly preferable as the microorganism classified as Dinoroseobacter; Phaeobacter gallaeciensis is particularly preferable as the microorganism classified as Phaeobacter; Octadecabacter antarcticus and Octadecabacter arcticus are particularly preferable as the microorganism classified as Octadecabacter; Hyphomonas neptunium is particularly preferable as the microorganism classified as Hyphomonas; Maricaulis maris is particularly preferable as the microorganism classified as Maricaulis; Hirschia baltica is particularly preferable as the microorganism classified as Hirschia; Sphingomonas paucimobilis and Sphingomonas wittichii are particularly preferable as the microorganism classified as Sphingomonas; Novosphingobium aromaticivorans is particularly preferable as the microorganism classified as Novosphingobium; Sphingopyxis alaskensis is particularly preferable as the microorganism classified as Sphingopyxis; Sphingobium japonicum and Sphingobium chlorophenolicum are particularly preferable as the microorganism classified as Sphingobium; Erythrobacter litoralis is particularly preferable as the microorganism classified as Erythrobacter; Brevundimonas diminuta, Brevundimonas subvibrioides and Brevundimonas vesicularis are particularly preferable as the microorganism classified as Brevundimonas; Caulobacter crescentus and Caulobacter segnis are particularly preferable as the microorganism classified as Caulobacter; Phenylobacterium zucineum is particularly preferable as the microorganism classified as Phenylobacterium; Asticcacaulis excentricus is particularly preferable as the microorganism classified as Asticcacaulis; Agrobacterium tumefaciens, Agrobacterium radiobacter and Agrobacterium luteum are particularly preferable as the microorganism classified as Agrobacterium; Rhizobium leguminosarum, Rhizobium etli and Rhizobium tropici are particularly preferable as the microorganism classified as Rhizobium; Sinorhizobium meliloti, Sinorhizobium medicae and Sinorhizobium fredii are particularly preferable as the microorganism classified as Sinorhizobium; Xanthobacter agilis, Xanthobacter aminoxidans, Xanthobacter autotrophicus, Xanthobacter flavus, Xanthobacter tagetidis and Xanthobacter viscosus are particularly preferable as the microorganism classified as Xanthobacter; Azorhizobium caulinodans is particularly preferable as the microorganism classified as Azorhizobium; Brucella melitensis, Brucella abortus, Brucella suis, Brucella ovis, Brucella canis, Brucella microti, Brucella pinnipedialis and Brucella ceti are particularly preferable as the microorganism classified as Brucella; Ochrobactrum anthropi, Ochrobactrum cytisi, Ochrobactrum daejeonense, Ochrobactrum gallinifaecis, Ochrobactrum grignonense, Ochrobactrum haemophilum, Ochrobactrum intermedium, Ochrobactrum lupini, Ochrobactrum oryzae, Ochrobactrum pseudintermedium, Ochrobactrum pseudogrignonense, Ochrobactrum thiophenivorans and Ochrobactrum tritici are particularly preferable as the microorganism classified as Ochrobactrum; Mesorhizobium alhagi, Mesorhizobium albiziae, Mesorhizobium amorphae, Mesorhizobium australicum, Mesorhizobium caraganae, Mesorhizobium chacoense, Mesorhizobium ciceri, Mesorhizobium gobiense, Mesorhizobium loti, Mesorhizobium mediterraneum, Mesorhizobium metallidurans, Mesorhizobium opportunistum, Mesorhizobium plurifarium, Mesorhizobium huakuii, Mesorhizobium septentrionale, Mesorhizobium shangrilense, Mesorhizobium tarimense, Mesorhizobium temperatum, Mesorhizobium thiogangeticu and Mesorhizobium tianshanense are particularly preferable as the microorganism classified as Mesorhizobium; Aurantimonas manganoxydans is particularly preferable as the microorganism classified as Aurantimonas; Bradyrhizobium japonicum is particularly preferable as the microorganism classified as Bradyrhizobium; Agromonas oligotrophica is particularly preferable as the microorganism classified as Agromonas; Rhodopseudomonas palustris is particularly preferable as the microorganism classified as Rhodopseudomonas; Nitrobacter winogradskyi and Nitrobacter hamburgensis are particularly preferable as the microorganism classified as Nitrobacter; Methylobacterium extorquens, Methylobacterium radiotolerans and Methylobacterium nodulans are particularly preferable as the microorganism classified as Methylobacterium; Rhodomicrobium vannielii is particularly preferable as the microorganism classified as Rhodomicrobium; Pelagibacterium halotolerans is particularly preferable as the microorganism classified as Pelagibacterium; Parvibaculum lavamentivorans is particularly preferable as the microorganism classified as Parvibaculum; Parvularcula bermudensis is particularly preferable as the microorganism classified as Parvularcula; Burkholderia mallei, Burkholderia pseudomallei, Burkholderia thailandensis, Burkholderia vietnamiensis, Burkholderia cenocepacia, Burkholderia ambifaria, Burkholderia multivorans, Burkholderia cepacia, Burkholderia xenovorans, Burkholderia phymatum, Burkholderia phytofirmans, Burkholderia glumae, Burkholderia rhizoxinica, Burkholderia gladioli, Burkholderia phenoliruptrix and Burkholderia oklahomensis are particularly preferable as the microorganism classified as Burkholderia; Ralstonia solanacearum, Ralstonia pickettii and Ralstonia eutropha are particularly preferable as the microorganism classified as Ralstonia; Cupriavidus metallidurans, Cupriavidus taiwanensis and Cupriavidus necator are particularly preferable as the microorganism classified as Cupriavidus; Polynucleobacter necessarius is particularly preferable as the microorganism classified as Polynucleobacter; Achromobacter arsenitoxydans, Achromobacter cholinophagum, Achromobacter cycloclastes, Achromobacter denitrificans, Achromobacter fischeri, Achromobacter hartlebii, Achromobacter immobilis, Achromobacter insolitus, Achromobacter lactolyticus, Achromobacter lyticus, Achromobacter methanolophila, Achromobacter pestifer, Achromobacter piechaudii, Achromobacter ruhlandii, Achromobacter spanios, Achromobacter viscosus, Achromobacter xerosis and Achromobacter xylosoxidans are particularly preferable as the microorganism classified as Achromobacter; Bordetella pertussis, Bordetella parapertussis, Bordetella petrii and Bordetella avium are particularly preferable as the microorganism classified as Bordetella; Taylorella equigenitalis is particularly preferable as the microorganism classified as Taylorella; Comamonas acidovorans, Comamonas aquatica, Comamonas badia, Comamonas composti, Comamonas denitrificans, Comamonas granuli, Comamonas kerstersii, Comamonas koreensis, Comamonas nitrativorans, Comamonas odontotermites, Comamonas terrae, Comamonas terrigena, Comamonas testosteroni, Comamonas thiooxydans and Comamonas zonglianii are particularly preferable as the microorganism classified as Comamonas; Alicycliphilus denitrificans is particularly preferable as the microorganism classified as Alicycliphilus; Delftia acidovorans is particularly preferable as the microorganism classified as Delftia; Ramlibacter tataouinensis is particularly preferable as the microorganism classified as Ramlibacter; Rhodoferax ferrireducens is particularly preferable as the microorganism classified as Rhodoferax; Variovorax paradoxus is particularly preferable as the microorganism classified as Variovorax; Polaromonas naphthalenivorans is particularly preferable as the microorganism classified as Polaromonas; Acidovorax citrulli, Acidovorax ebreus and Acidovorax avenae are particularly preferable as the microorganism classified as Acidovorax; Verminephrobacter eiseniae is particularly preferable as the microorganism classified as Verminephrobacter; Herminiimonas arsenicoxydans is particularly preferable as the microorganism classified as Herminiimonas; Herbaspirillum seropedicae is particularly preferable as the microorganism classified as Herbaspirillum; Collimonas fungivorans is particularly preferable as the microorganism classified as Collimonas; Chromobacterium violaceum is particularly preferable as the microorganism classified as Chromobacterium; Laribacter hongkongensis is particularly preferable as the microorganism classified as Laribacter; Pseudogulbenkiania ferrooxidans is particularly preferable as the microorganism classified as Pseudogulbenkiania; Nitrosomonas europaea is particularly preferable as the microorganism classified as Nitrosomonas; Nitrosospira multiformis is particularly preferable as the microorganism classified as Nitrosospira; Aromatoleum aromaticumis particularly preferable as the microorganism classified as Aromatoleum; Dechloromonas aromatica is particularly preferable as the microorganism classified as Dechloromonas; Azospira oryzae (Dechlorosoma suillum) is particularly preferable as the microorganism classified as Azospira (Dechlorosoma); Rheinheimera nanhaiensis is particularly preferable as the microorganism classified as Rheinheimera; Nitrosococcus oceani is particularly preferable as the microorganism classified as Nitrosococcus; Halorhodospira halophila is particularly preferable as the microorganism classified as Halorhodospira; Xanthomonas campestris, Xanthomonas axonopodis, Xanthomonas oryzae, Xanthomonas albilineans and Xanthomonas citri are particularly preferable as the microorganism classified as Xanthomonas; Stenotrophomonas maltophilia is particularly preferable as the microorganism classified as Stenotrophomonas; Pseudoxanthomonas suwonensis and Pseudoxanthomonas spadix are particularly preferable as the microorganism classified as Pseudoxanthomonas; Francisella tularensis and Francisella novicida are particularly preferable as the microorganism classified as Francisella; Cycloclasticus zancles is particularly preferable as the microorganism classified as Cycloclasticus; Hahella chejuensis is particularly preferable as the microorganism classified as Hahella; Halomonas elongata is particularly preferable as the microorganism classified as Halomonas; Alcanivorax borkumensis and Alcanivorax dieselolei are particularly preferable as the microorganism classified as Alcanivorax; Kangiella koreensis is particularly preferable as the microorganism classified as Kangiella; Pseudomonas aeruginosa, Pseudomonas putida, Pseudomonas fluorescens, Pseudomonas agarici, Pseudomonas syringae, Pseudomonas amygdale and Pseudomonas stutzeri, for example, are particularly preferable as the microorganism classified as Pseudomonas; Azotobacter vinelandii is particularly preferable as the microorganism classified as Azotobacter; Acinetobacter baumannii, Acinetobacter aylyi, Acinetobacter calcoaceticus, Acinetobacter gyllenbergii, Acinetobacter haemolyticus, Acinetobacter johnsonii, Acinetobacter junii, Acinetobacter lwoffii, Acinetobacter oleivorans and Acinetobacter parvus are particularly preferable as the microorganism classified as Acinetobacter; Psychrobacter arcticus and Psychrobacter cryohalolentis are particularly preferable as the microorganism classified as Psychrobacter; Alishewanella jeotgali is particularly preferable as the microorganism classified as Alishewanella; Alteromonas macleodii is particularly preferable as the microorganism classified as Alteromonas; Glaciecola nitratireducens, Glaciecola psychrophila and Glaciecola punicea are particularly preferable as the microorganism classified as Glaciecola; Marinobacter aquaeolei, Marinobacter hydrocarbonoclasticus, Marinobacter adhaerens, Marinobacter algicola and Marinobacter manganoxydans are particularly preferable as the microorganism classified as Marinobacter; Marinobacterium stanieri is particularly preferable as the microorganism classified as Marinobacterium; Saccharophagus degradans is particularly preferable as the microorganism classified as Saccharophagus; Shewanella piezotolerans, Shewanella abyssi, Shewanella affinis, Shewanella algae, Shewanella algidipiscicola, Shewanella amazonensis, Shewanella aquimarina, Shewanella arctica, Shewanella atlantica, Shewanella baltica, Shewanella basaltis, Shewanella benthica, Shewanella candadensis, Shewanella chilikensis, Shewanella colwelliana, Shewanella corallii, Shewanella decolorationis, Shewanella denitrificans, Shewanella donghaensis, Shewanella fidelis, Shewanella fodinae, Shewanella frigidimarina, Shewanella gaetbuli, Shewanella gelidimarina, Shewanella glacialipiscicola, Shewanella gopherii, Shewanella hafniensis, Shewanella halifaxensis, Shewanella haliotis, Shewanella hanedai, Shewanella japonica, Shewanella kaireitica, Shewanella ivingstonensis, Shewanella loihica, Shewanella marina, Shewanella marinintestina, Shewanella marisflavi, Shewanella morhuae, Shewanella olleyana, Shewanella oneidensis, Shewanella pacifica, Shewanella pealeana, Shewanella pneumatophori, Shewanella profunda, Shewanella putrefaciens, Shewanella sairae, Shewanella schlegeliana, Shewanella sediminis, Shewanella surugensis, Shewanella vesiculosa, Shewanella violacea, Shewanella waksmanii, Shewanella woodyi and Shewanella xiamenensis are particularly preferable as the microorganism classified as Shewanella; Ferrimonas balearica is particularly preferable as the microorganism classified as Ferrimonas; Idiomarina loihiensis and Idiomarina baltica are particularly preferable as the microorganism classified as Idiomarina; Colwellia psychrerythraea is particularly preferable as the microorganism classified as Colwellia; Pseudoalteromonas haloplanktis, Pseudoalteromonas atlantica and Pseudoalteromonas tunicata are particularly preferable as the microorganism classified as Pseudoalteromonas; Listonella anguillara, Listonella anguillarum and Listonella pelagia are particularly preferable as the microorganism classified as Listonella; Vibrio parahaemolyticus, Vibrio vulnificus, Vibrio harveyi, Vibrio furnissii, Vibrio tubiashii, Vibrio sinaloensis, Vibrio rotiferianus, Vibrio orientalis, Vibrio harveyi, Vibrio coralliilyticus, Vibrio caribbenthicus, Vibrio brasiliensis and Vibrio alginolyticus are particularly preferable as the microorganism classified as Vibrio; Photobacterium profundum is particularly preferable as the microorganism classified as Photobacterium; Aeromonas hydrophila, Aeromonas salmonicida and Aeromonas veronii are particularly preferable as the microorganism classified as Aeromonas; Salinisphaera shabanensis is particularly preferable as the microorganism classified as Salinisphaera; Legionella pneumophila and Legionella longbeachae are particularly preferable as the microorganism classified as Legionella; Coxiella burnetii is particularly preferable as the microorganism classified as Coxiella; Desulfococcus oleovorans is particularly preferable as the microorganism classified as Desulfococcus; Desulfobacterium autotrophicum is particularly preferable as the microorganism classified as Desulfobacterium; Desulfatibacillum alkenivorans is particularly preferable as the microorganism classified as Desulfatibacillum; Desulfobulbus propionicus is particularly preferable as the microorganism classified as Desulfobulbus; Desulfarculus baarsii is particularly preferable as the microorganism classified as Desulfarculus; Geobacter metallireducens, Geobacter uraniireducens and Geobacter bemidjiensis are particularly preferable as the microorganism classified as Geobacter; Syntrophobacter fumaroxidans is particularly preferable as the microorganism classified as Syntrophobacter; Syntrophus aciditrophicus is particularly preferable as the microorganism classified as Syntrophus; Desulfomonile tiedjei is particularly preferable as the microorganism classified as Desulfomonile; Bdellovibrio bacteriovorus and Bdellovibrio exovorus are particularly preferable as the microorganism classified as Bdellovibrio; Bacteriovorax marinus is particularly preferable as the microorganism classified as Bacteriovorax; Stigmatella aurantiaca is particularly preferable as the microorganism classified as Stigmatella; Myxococcus xanthus and Myxococcus fulvus are particularly preferable as the microorganism classified as Myxococcus; Anaeromyxobacter dehalogenans is particularly preferable as the microorganism classified as Anaeromyxobacter; Sorangium cellulosum is particularly preferable as the microorganism classified as Sorangium; Haliangium ochraceum is particularly preferable as the microorganism classified as Haliangium; Acidobacterium capsulatum is particularly preferable as the microorganism classified as Acidobacterium; Granulicella tundricola is particularly preferable as the microorganism classified as Granulicella; Ilumatobacter coccineum is particularly preferable as the microorganism classified as Ilumatobacter; Streptosporangium roseum is particularly preferable as the microorganism classified as Streptosporangium; Nocardiopsis dassonvillei is particularly preferable as the microorganism classified as Nocardiopsis; Thermobifida fusca is particularly preferable as the microorganism classified as Thermobifida; Thermomonospora curvata is particularly preferable as the microorganism classified as Thermomonospora; Pseudonocardia dioxanivorans is particularly preferable as the microorganism classified as Pseudonocardia; Amycolatopsis mediterranei is particularly preferable as the microorganism classified as Amycolatopsis; Saccharomonospora viridis and Saccharomonospora xinjiangensis are particularly preferable as the microorganism classified as Saccharomonospora; Saccharopolyspora erythraea and Saccharopolyspora spinosa are particularly preferable as the microorganism classified as Saccharopolyspora; Thermobispora bispora is particularly preferable as the microorganism classified as Thermobispora; Actinosynnema mirum is particularly preferable as the microorganism classified as Actinosynnema; Micromonospora aurantiaca is particularly preferable as the microorganism classified as Micromonospora; Salinispora tropica and Salinispora arenicola are particularly preferable as the microorganism classified as Salinispora; Verrucosispora maris is particularly preferable as the microorganism classified as Verrucosispora; Kribbella flavida is particularly preferable as the microorganism classified as Kribbella; Corynebacterium jeikeium, Corynebacterium urealyticum and Corynebacterium kroppenstedtii are particularly preferable as the microorganism classified as Corynebacterium; Nocardia farcinica, Nocardia brasiliensis and Nocardia cyriacigeorgica are particularly preferable as the microorganism classified as Nocardia; Rhodococcus rhodochrous, Rhodococcus erythropolis, Rhodococcus equi, Rhodococcus rhodnii, Rhodococcus corallinus, Rhodococcus rubropertinctus, Rhodococcus coprophilus, Rhodococcus globerulus, Rhodococcus chlorophenolicus, Rhodococcus luteus, Rhodococcus aichiensis, Rhodococcus chubuensis, Rhodococcus maris and Rhodococcus fascines are particularly preferable as the microorganism classified as Rhodococcus; Gordonia bronchialis, Gordonia neofelifaecis and Gordonia terrae are particularly preferable as the microorganism classified as Gordonia; Dietzia cinnamea is particularly preferable as the microorganism classified as Dietzia; Mycobacterium tuberculosis, Mycobacterium bovis, Mycobacterium leprae, Mycobacterium avium, Mycobacterium smegmatis, Mycobacterium ulcerans, Mycobacterium vanbaalenii, Mycobacterium gilvum, Mycobacterium abscessus, Mycobacterium marinu, Mycobacterium massiliense, Mycobacterium phlei, Mycobacterium thermoresistibile, Mycobacterium tusciae, Mycobacterium xenopi and Mycobacterium rhodesiae are particularly preferable as the microorganism classified as Mycobacterium; Amycolicicoccus subflavus is particularly preferable as the microorganism classified as Amycolicicoccus; Tsukamurella paurometabola is particularly preferable as the microorganism classified as Tsukamurella; Segniliparus rotundus is particularly preferable as the microorganism classified as Segniliparus; Microbacterium testaceum is particularly preferable as the microorganism classified as Microbacterium; Micrococcus luteus is particularly preferable as the microorganism classified as Micrococcus; Arthrobacter arilaitensis, Arthrobacter chlorophenolicus, Arthrobacter globiformis and Arthrobacter phenanthrenivorans are particularly preferable as the microorganism classified as Arthrobacter; Renibacterium salmoninarum is particularly preferable as the microorganism classified as Renibacterium; Kocuria rhizophila is particularly preferable as the microorganism classified as Kocuria; Kytococcus sedentarius is particularly preferable as the microorganism classified as Kytococcus; Cellulomonas fimi is particularly preferable as the microorganism classified as Cellulomonas; Intrasporangium calvum is particularly preferable as the microorganism classified as Intrasporangium; Serinicoccus profundi is particularly preferable as the microorganism classified as Serinicoccus; Frankia alni is particularly preferable as the microorganism classified as Frankia; Acidothermus cellulolyticus is particularly preferable as the microorganism classified as Acidothermus; Nakamurella multipartita is particularly preferable as the microorganism classified as Nakamurella; Geodermatophilus obscurus is particularly preferable as the microorganism classified as Geodermatophilus; Stackebrandtia nassauensis is particularly preferable as the microorganism classified as Stackebrandtia; Streptomyces albus, Streptomyces avermitilis, Streptomyces bingchenggensis, Streptomyces chartreusis, Streptomyces clavuligerus, Streptomyces coelicoflavus, Streptomyces coelicolor, Streptomyces ghanaensis, Streptomyces griseus, Streptomyces hygroscopicus, Streptomyces lividans, Streptomyces roseosporus, Streptomyces scabiei, Streptomyces sviceus, Streptomyces venezuelae, Streptomyces violaceusniger and Streptomyces viridochromogenes are particularly preferable as the microorganism classified as Streptomyces; Catenulispora acidiphila is particularly preferable as the microorganism classified as Catenulispora; Rubrobacter xylanophilus is particularly preferable as the microorganism classified as Rubrobacter; Conexibacter woesei is particularly preferable as the microorganism classified as Conexibacter; Bacillus thuringiensis, Bacillus megaterium, Bacillus pseudofirmus, Bacillus clausii, Bacillus cereus, Bacillus subtilis and Bacillus thuringiensis are particularly preferable as the microorganism classified as Bacillus; Geobacillus caldoproteolyticus, Geobacillus caldoxylosilyticus, Geobacillus debilis, Geobacillus galactosidasius, Geobacillus gargensis, Geobacillus jurassicus, Geobacillus kaustophilus, Geobacillus lituanicus, Geobacillus pallidus, Geobacillus stearothermophilus, Geobacillus stromboliensis, Geobacillus subterraneus, Geobacillus tepidamans, Geobacillus thermocatenulatus, Geobacillus thermodenitrificans, Geobacillus thermoglucosidasius, Geobacillus thermoleovorans, Geobacillus toebii, Geobacillus uzensis, Geobacillus vulcani and Geobacillus zalihae are particularly preferable as the microorganism classified as Geobacillus; Oceanobacillus iheyensis is particularly preferable as the microorganism classified as Oceanobacillus; Lysinibacillus sphaericus is particularly preferable as the microorganism classified as Lysinibacillus; Halobacillus halophilus is particularly preferable as the microorganism classified as Halobacillus; Alicyclobacillus acidocaldarius is particularly preferable as the microorganism classified as Alicyclobacillus; Kyrpidia tusci is particularly preferable as the microorganism classified as Kyrpidia; Paenibacillus polymyxa, Paenibacillus mucilaginosus and Paenibacillus terrae are particularly preferable as the microorganism classified as Paenibacillus; Lactobacillus buchneri is particularly preferable as the microorganism classified as Lactobacillus; Clostridium acetobutylicum, Clostridium perfringens, Clostridium kluyveri, Clostridium cellulovorans, Clostridium difficile and Clostridium sticklandii are particularly preferable as the microorganism classified as Clostridium; Alkaliphilus metalliredigens and Alkaliphilus oremlandii are particularly preferable as the microorganism classified as Alkaliphilus; Syntrophomonas wolfei is particularly preferable as the microorganism classified as Syntrophomonas; Syntrophothermus lipocalidus is particularly preferable as the microorganism classified as Syntrophothermus; Eubacterium rectale and Eubacterium limosum are particularly preferable as the microorganism classified as Eubacterium; Desulfitobacterium hafniense is particularly preferable as the microorganism classified as Desulfitobacterium; Desulfotomaculum reducens is particularly preferable as the microorganism classified as Desulfotomaculum; Pelotomaculum thermopropionicum is particularly preferable as the microorganism classified as Pelotomaculum; Butyrivibrio proteoclasticus is particularly preferable as the microorganism classified as Butyrivibrio; Roseburia hominis is particularly preferable as the microorganism classified as Roseburia; Oscillibacter valericigenes is particularly preferable as the microorganism classified as Oscillibacter; Thermoanaerobacter tengcongensis is particularly preferable as the microorganism classified as Thermoanaerobacter; Carboxydothermus hydrogenoformans is particularly preferable as the microorganism classified as Carboxydothermus; Natranaerobius thermophilus is particularly preferable as the microorganism classified as Natranaerobius; Sphingobacterium multivorum, Sphingobacterium spiritivorum, Sphingobacterium alimentarium, Sphingobacterium anhuiense, Sphingobacterium antarcticum, Sphingobacterium bambusae, Sphingobacterium canadense, Sphingobacterium composti, Sphingobacterium daejeonense, Sphingobacterium faecium, Sphingobacterium heparinum, Sphingobacterium kitahiroshimense, Sphingobacterium lactis, Sphingobacterium mizutaii, Sphingobacterium nematocida, Sphingobacterium piscium, Sphingobacterium shayense, Sphingobacterium siyangense, Sphingobacterium thalpophilum and Sphingobacterium wenxiniae are particularly preferable as the microorganism classified as Sphingobacterium; Pedobacter steynii, Pedobacter duraquae, Pedobacter metabolipauper, Pedobacter hartonius, Pedobacter heparinus Pedobacter africanus, Pedobacter agri, Pedobacter alluvius and Pedobacter saltans are particularly preferable as the microorganism classified as Pedobacter; Haliscomenobacter hydrossis is particularly preferable as the microorganism classified as Haliscomenobacter; Porphyromonas gingivalis and Porphyromonas asaccharolytica are particularly preferable as the microorganism classified as Porphyromonas; Odoribacter splanchnicus is particularly preferable as the microorganism classified as Odoribacter; Spirosoma linguale is particularly preferable as the microorganism classified as Spirosoma; Runella slithyformis is particularly preferable as the microorganism classified as Runella; Deinococcus radiodurans, Deinococcus geothermalis, Deinococcus deserti, Deinococcus maricopensis, Deinococcus proteolyticus and Deinococcus gobiensis are particularly preferable as the microorganism classified as Deinococcus; Thermus thermophilus and Thermus scotoductusis particularly preferable as the microorganism classified as Thermus; Meiothermus ruber and Meiothermus silvanus are particularly preferable as the microorganism classified as Meiothermus; Oceanithermus profundus is particularly preferable as the microorganism classified as Oceanithermus; Marinithermus hydrothermalis is particularly preferable as the microorganism classified as Marinithermus; Gemmatimonas aurantiaca is particularly preferable as the microorganism classified as Gemmatimonas; Fusobacterium nucleatum is particularly preferable as the microorganism classified as Fusobacterium; Ilyobacter polytropus is particularly preferable as the microorganism classified as Ilyobacter; Roseiflexus castenholzii is particularly preferable as the microorganism classified as Roseiflexus; Herpetosiphon aurantiacus is particularly preferable as the microorganism classified as Herpetosiphon; Thermomicrobium roseum is particularly preferable as the microorganism classified as Thermomicrobium; Thermotoga lettingae is particularly preferable as the microorganism classified as Thermotoga; Thermosipho melanesiensis and Thermosipho africanus are particularly preferable as the microorganism classified as Thermosipho; Fervidobacterium nodosum is particularly preferable as the microorganism classified as Fervidobacterium; Deferribacter desulfuricans is particularly preferable as the microorganism classified as Deferribacter; Calditerrivibrio nitroreducens is particularly preferable as the microorganism classified as Calditerrivibrio; Flexistipes sinusarabici is particularly preferable as the microorganism classified as Flexistipes; Metallosphaera sedula is particularly preferable as the microorganism classified as Metallosphaera; Aeropyrum pernix is particularly preferable as the microorganism classified as Aeropyrum; Pyrobaculum aerophilum, Pyrobaculum islandicum, Pyrobaculum calidifontis and Pyrobaculum neutrophilum are particularly preferable as the microorganism classified as Pyrobaculum; Caldivirga maquilingensis is particularly preferable as the microorganism classified as Caldivirga; Vulcanisaeta distributa is particularly preferable as the microorganism classified as Vulcanisaeta; Acidilobus saccharovorans is particularly preferable as the microorganism classified as Acidilobus; Haloarcula marismortui is particularly preferable as the microorganism classified as Haloarcula; Haloquadratum walsbyi is particularly preferable as the microorganism classified as Haloquadratum; Natronomonas pharaonis is particularly preferable as the microorganism classified as Natronomonas; Halorubrum lacusprofundi is particularly preferable as the microorganism classified as Halorubrum; Haloterrigena turkmenica is particularly preferable as the microorganism classified as Haloterrigena; Natrialba magadii is particularly preferable as the microorganism classified as Natrialba; Halalkalicoccus jeotgali is particularly preferable as the microorganism classified as Halalkalicoccus; Halogeometricum borinquense is particularly preferable as the microorganism classified as Halogeometricum; Thermoplasma acidophilum and Thermoplasma volcanium are particularly preferable as the microorganism classified as Thermoplasma; Picrophilus torridus is particularly preferable as the microorganism classified as Picrophilus; Ferroplasma acidarmanus is particularly preferable as the microorganism classified as Ferroplasma; Archaeoglobus fulgidus and Archaeoglobus veneficus are particularly preferable as the microorganism classified as Archaeoglobus; Ferroglobus placidus is particularly preferable as the microorganism classified as Ferroglobus; Polymorphum gilvum is particularly preferable as the microorganism classified as Polymorphum; Micavibrio aeruginosavorus is particularly preferable as the microorganism classified as Micavibrio; Simiduia agarivorans is particularly preferable as the microorganism classified as Simiduia; Leptothrix cholodnii is particularly preferable as the microorganism classified as Leptothrix; Thiomonas intermedia is particularly preferable as the microorganism classified as Thiomonas; Rubrivivax gelatinosus is particularly preferable as the microorganism classified as Rubrivivax; Methylibium petroleiphilum is particularly preferable as the microorganism classified as Methylibium; and Anaerococcus prevotii is particularly preferable as the microorganism classified as Anaerococcus.
The microorganisms exemplified herein are obtainable from the American Type Culture Collection (ATCC), National Institute of Technology and Evaluation, Biotechnology Division, Biological Resource Center (NBRC), National Institute of Advanced Industrial Science and Technology, Patent Organism Depository (FERM), or the like.
Synthesis Process of Methacrylic Acid Ester
The production of methacrylic acid ester can be performed by the following method. A solution was prepared by adding alcohol or phenol represented by Formula 2 and methacrylyl-CoA to a solvent, and then allowing to dissolve or suspend. Then, AAT is brought into contact with this solution or suspension, and methacrylyl-CoA and the alcohol or phenol is allowed to react while controlling conditions such as temperature. By way of the reaction, a methacrylic group of methacrylyl-CoA is transferred to the alcohol or phenol of Formula 2, thereby causing methacrylic acid ester to be formed.
The solution containing the methacrylyl-CoA and alcohol or phenol represented by Formula 2 is normally prepared in an aqueous medium such as a buffer solution. Herein, in order to cause the reaction to progress smoothly, it is possible to control the osmolar concentration and/or ion strength by way of an osmotic pressure regulator or the like. As the osmotic pressure regulator, it is sufficient if a water-soluble substance added with the object of adjusting the osmotic pressure of the solution such as the inside of the cell so as to make isotonic or hypertonic, and for example, is a salt or saccharide, and preferably a salt. The salt is preferably a metallic salt, more preferably an alkali metal salt, even more preferably an alkali metal halide, and for example, sodium chloride and potassium chloride can be exemplified. The saccharide is preferably a monosaccharide or oligosaccharide, more preferably a monosaccharide or disaccharide, and for example, glucose, sucrose, mannitol and the like can be exemplified. The osmotic pressure regulator is preferably added at a concentration of at least 1 mM, and it is particularly preferable to regulate so as to make isotonic or hypertonic compared to a solution inside the biological cell used.
In addition, with the object of separating the methacrylic acid ester thus formed, an organic solvent can be added in advance to make react in a two-phase system. As the organic solvent, for example, a linear, branched or cyclic, saturated or unsaturated aliphatic hydrocarbon, saturated or unsaturated aromatic hydrocarbon, or the like can be used individually or by mixing two or more types. More specifically, for example, hydrocarbon solvents (e.g., pentane, hexane, cyclohexane, benzene, toluene, xylene, etc.), halogenated hydrocarbon solvents (e.g., methylene chloride, chloroform, etc.), ether solvents (e.g., diethyl ether, dipropyl ether, dibutyl ether, tert-butylmethyl ether, dimethoxyethane, etc.), ester solvents (e.g., methyl formate, methyl acetate, ethyl acetate, butyl acetate, methyl propionate), and the like can be exemplified. By adding these organic solvents, the methacrylic acid ester formed will migrate to the organic phase, and the reaction may progress efficiently.
The molar ratios and concentrations of methacrylyl-CoA and the alcohol or phenol represented by Formula 2 in the reaction solution are arbitrary, and not particularly limited. In addition, the amount of AAT used or reaction conditions are determined as appropriate according to the raw materials used. Usually, the concentration of each raw material is set to the range of 0.0000001 to 10% by mass in the case of methacrylyl-CoA, and the alcohol or phenol is added at a concentration of 0.1 to 1000 times by moles, preferably 0.5 to 50 times by moles, relative to the methacrylyl-CoA used.
Various other conditions such as the reaction temperature or reaction time are determined as appropriate according to the raw materials used, activity of enzyme, etc., and are not particularly limited; however, it is sufficient normally if allowed to react at 5 to 80° C. for 1 hour to 1 week. At 10 to 70° C., it is preferably for 1 to 120 hours, more preferably at least 3 hours, and 4 or more hours is even more preferable. It is preferable to select conditions by which the reaction completes at such conditions. The pH of the reaction solution is not particularly limited so long as the reaction efficiently progresses; however, for example, it is a range of pH 4 to 10, and preferably pH 5.5 to 8.5.
As ideal conditions for causing methacrylic acid ester to collect in at least 0.001 mM, preparing so that the concentration of methacrylyl-CoA under the condition of pH 5.5 to 7.5 is in the range of 0.000001 to 1% by mass directly or indirectly, and the alcohol or phenol is adjusted to a concentration so as to be 1 to 50 times by moles relative to the methacrylyl-CoA used. Then, the temperature is adjusted to the range of 20 to 40° C., and reaction is allowed for at least 3 hours. It is also possible to continuously supply these raw materials (substrate) so as to be in the aforementioned ranges, and the accumulation concentration of product can be raised by doing so.
Conducting the present reaction under reduced pressure or aeration conditions is also effective. It is because, under these conditions, the methacrylic acid ester thus formed can be continuously separated, a result of which the reaction may progress efficiently.
In the case of producing methacrylic acid ester using methacrylyl-CoA transformed by action of ACD with isobutyryl-CoA as the raw material or methacrylyl-CoA transformed by action of ECH from 3-hydroxyisobutyryl-CoA, it is preferable to implement by adjusting so as to be in the range of these conditions. It should be noted that the methacrylyl-CoA synthesis reaction from ACD or ECH can be conducted by a known method (for example, as reaction conditions for ACD, the conditions described in Microbiology (1999), 145, pp. 2323-2334). By combining with yet another biological reaction, continuous reaction (fermentative production) within an organism for methacrylic acid ester becomes possible.
The methacrylic acid ester formed by the method of the present invention can be qualitatively or quantitatively analyzed by way of gas chromatography (GC), high performance liquid chromatography (HPLC), or the like as necessary.
Isolation of methacrylic acid ester from the reaction solution can be performed by an individual or combination of known purification methods such as distillation, thin-film distillation, solvent extraction and column separation. In addition, the obtained methacrylic acid ester can polymerize by a typical method, and used without inferiority in conventional uses.
The methacrylic acid ester obtained in this way or polymer thereof can remarkably reduce the energy, resources and load on the environment, and has an extremely great social value as a low-environmental load material compared to conventional chemicals with petroleum products as starting materials.
2. Method for Producing Methacrylic Acid Ester from Precursor by Genetically Modified Microorganism
Recombinant Microorganism Having Methacrylic Acid Ester Formability from Precursor
As mentioned in the foregoing, with the present invention, it is also possible to synthesize methacrylic acid ester from a precursor such as isobutyryl-CoA, 3-hydroxyisobutyryl-CoA or 2-isovaleric acid, by introducing ACD gene, ECH gene, BCKAD gene or the like as necessary to a microorganism to which AAT gene has been introduced.
“Precursor” indicates a compound that is inducible to methacrylyl-CoA, and indicates isobutyryl-CoA or 3-hydroxyisobutyryl-CoA, and further, the matter of a substance inducible to these two compounds. As the substance inducible to two compounds, for example, acids such as 2-oxoisovaleric acid, isobutyric acid, 3-hydroxy isobutyric acid, acetic acid, pyruvic acid, lactic acid, acetoacetic acid, butyric acid, propionic acid, malic acid, fumaric acid, citric acid and succinic acid; amino acids such as valine, alanine, leucine, lysine and glutamic acid; and saccharides such as glucose, fructose and xylose can be exemplified.
To cause methacrylic acid ester to form from these precursors, it is also possible to utilize various metabolic pathways naturally possessed by the host microorganism. Genes can be introduced or made deficient as necessary.
(1) Host Microorganism
As the host microorganism, it is not particularly limited so long as being a host having enzymes for forming methacrylyl-CoA from the precursor and expression capability of AAT; however, as for bacterium, Rhodococcus, Pseudomonas, Corynebacterium, Bacillus, Streptococcus, Streptomyces, etc. can be exemplified, as for yeast, Saccharomyces, Candida, Shizosaccharomyces and Pichia, and as for filamentous fungus, Aspergillus, etc. can be exemplified.
A microorganism of Rhodococcus genus is preferable as the host. The reason thereof is because of the knowledge arrived at by experimentally confirming in the course of the present invention that a microorganism of Rhodococcus genus has valine assimilativity, and finding that, by utilizing this function, it is possible to apply to methacrylic acid ester formation by the route shown in FIG. 2.
For example, one type selected from the following microorganisms can be used individually, or by combining two or more types. As microorganisms classified as Rhodococcus sp., for example, Rhodococcus rhodochrous, Rhodococcus erythropolis, Rhodococcus equi, Rhodococcus rhodnii, Rhodococcus corallinus, Rhodococcus rubropertinctus, Rhodococcus coprophilus, Rhodococcus globerulus, Rhodococcus chlorophenolicus, Rhodococcus luteus, Rhodococcus aichiensis, Rhodococcus chubuensis, Rhodococcus maris, Rhodococcus fascines and the like can be exemplified.
As a preferred example, Rhodococcus erythropolis can be exemplified. As more preferred strains, Rhodococcus erythropolis strain PR-4, Rhodococcus erythropolis strain KA2-5-1, Rhodococcus erythropolis strain IGTS8, Rhodococcus erythropolis strain D-1, Rhodococcus erythropolis strain H-2, Rhodococcus erythropolis strain N1-36, Rhodococcus erythropolis strain 1-19, Rhodococcus erythropolis strain ECRD-1, Rhodococcus erythropolis strain B1, Rhodococcus erythropolis strain SY-1, Rhodococcus erythropolis strain UM3, Rhodococcus erythropolis strain UM9, Rhodococcus equi strain T09, or the like can be exemplified, and particularly preferably, Rhodococcus erythropolis strain PR-4 can be exemplified. Furthermore, derivatives of these strains are included.
As derivatives, variant strains obtained by inducing gene mutation in a microorganism having methacrylyl-CoA formability by way of a change in culture conditions (e.g., medium composition, temperature, etc.), chemical or physical treatment (e.g., γ radiation, etc.), genetically modified strains for which activity has been enhanced in the following way, or activity has been made deficient or reduced are included.
Activity enhancement indicates the expression level of enzyme gene (irrespective of origin) increasing in the microorganism based on the gene introduced from outside the bacterial cell to the microorganism, and in addition to introducing genes encoding enzymes from outside the bacterial cell of the microorganism to inside the bacterial cell, includes enhancing the enzyme activity as a result of causing the enzyme gene to be highly expressed by enhancing the promoter activity of the enzyme gene retained on the genome by the microorganism, or substituting with another promoter, or alternatively, reducing or inactivating the repressor activity of the enzyme gene.
The genetically modified strain may be a modified strain arrived at by performing genetic modification causing the activity of enzyme inhibiting the methacrylyl-CoA synthesis reaction to be knocked out or decreased. Activity “deficient” or “decrease” indicates the expression of the enzyme gene being entirely lost or reduced in this microorganism, and in addition to substitution, deletion or insertion occurring for this enzyme gene, includes decreasing the enzyme activity as a result of suppressing the expression of enzyme gene by decreasing the promoter activity of an enzyme gene retained on the genome by the microorganism or substituting with another promoter, or alternatively enhancing or activating the repressor activity of this enzyme gene. It should be noted that these genetic modifications may be performed following a conventional method.
As a preferred modified strain in the case of conducting methacrylic acid ester production by the route shown in FIG. 2, a modified strain having at least one characteristic of (a) or (b) shown below can be exemplified.
    • (a) Methacrylyl-CoA formation activity is being enhanced by BCKAD gene and/or ACD gene being introduced.
    • (b) Methacrylyl-CoA formation activity is being enhanced by knock out or inactivation of ECH gene, 3-hydroxy isobutyryl-CoA hydrolase gene and/or 3-hydroxy isobutyric acid dehydrogenase gene. Knock out or deactivation is performed by substituting, deleting or inserting an entirety of the gene or part of the nucleotide sequence.
      (2) Inserted Gene
It becomes necessary to introduce respective genes of enzymes for forming methacrylyl-CoA from the precursor and AAT gene as necessary to the host. Various enzymes naturally possessed by the host microorganism can be utilized as is. Alternatively, it is also possible to enhance activity by way of gene introduction as necessary.
According to the host and synthesis route, the enzyme for forming methacrylyl-CoA from the precursor is selected as appropriate or optimized, and is not particularly limited; however, hereinafter, the necessary enzyme genes for methacrylic acid ester formation by the route shown in FIG. 2 will be described in detail using a microorganism of Rhodococcus genus as the host.
(2-1) Alcohol Acyltransferase (AAT)
The AAT used in the present invention is not particularly limited so long as having ability to produce methacrylic acid ester with methacrylyl-CoA and alcohol or phenol as raw materials, and the kind and origin thereof are not of concern. One of plant origin is preferable as the enzyme source, and as representative sources thereof, those originating from any order selected from the group consisting of the aforementioned Zingiberales, Rosales, Ericales, Cucurbitales, Brassicales and Laurales can be exemplified.
(2-2) Acyl-CoA Dehydrogenase (ACD)
The ACD used in the present invention is not particularly limited so long as having an ability to form methacrylyl-CoA from acyl-CoA, and the source and type thereof are not of concern. Those derived from microorganism are preferable, and representative ones are as shown before.
More preferably, it is derived from Rhodococcus erythropolis, and as preferred strains, Rhodococcus erythropolis strain PR-4, Rhodococcus erythropolis strain KA2-5-1, Rhodococcus erythropolis strain IGTS8, Rhodococcus erythropolis strain D-1, Rhodococcus erythropolis strain H-2, Rhodococcus erythropolis strain N1-36, Rhodococcus erythropolis strain 1-19, Rhodococcus erythropolis strain ECRD-1, Rhodococcus erythropolis strain B1, Rhodococcus erythropolis strain SY-1, Rhodococcus erythropolis strain UM3, Rhodococcus erythropolis strain UM9, Rhodococcus equi strain T09, or the like can be exemplified, and particularly preferably, Rhodococcus erythropolis strain PR-4 can be exemplified.
The nucleotide sequence of ACD gene derived from Rhodococcus erythropolis strain PR-4 is shown in SEQ ID NO. 33, and the amino acid sequence coded by this nucleotide sequence is shown in SEQ ID NO. 32. It should be noted that amino acid sequences in which one or a plurality of amino acids in the amino acid sequence shown in SEQ ID NO. 32 have been substituted, deleted or added are included, and genes coding proteins having activity to form methacrylyl-CoA from acyl-CoA are also included in the ACD gene of the present invention. In addition, in the ACD gene of the present invention, genes coding protein having activity to produce methacrylic acid ester from acyl-CoA expressing at least 90% identity with the protein consisting of the amino acid sequence shown by SEQ ID NO. 32, preferably at least 95%, more preferably at least 99.5%, and even more preferably at least 99.9% are also included.
Furthermore, in the ACD gene of the present invention, genes hybridizing under stringent conditions to a polynucleotide having the complementary nucleotide sequence to the nucleotide sequence shown by SEQ ID NO. 33, and coding proteins having activity to form methacrylic acid ester from acyl-CoA are also included. Furthermore, in the ACD gene of the present invention, when calculating using the nucleotide sequence shown in SEQ ID NO. 33, BLAST, etc. (e.g., default, i.e. initial setting, parameters), genes coding proteins having activity to form methacrylic acid ester from acyl-CoA and alcohol consisting of a nucleotide sequence having identity of at least 80%, more preferably at least 90%, and most preferably at least 95% are also included. In addition, the codons of the above-mentioned ACD gene may be changed according to the codon frequency of use in the microorganism used in transformation.
DNA coding the above-mentioned AAT gene and/or ACD gene is introduced to a microorganism belonging to Rhodococcus sp., and used to cause transcription/translation to proteins in this microorganism. The DNA introduced to this microorganism is preferably in the form incorporated in a vector.
(3) Preparation of Recombinant Microorganism
DNA coding the above-mentioned AAT gene and/or ACD gene is introduced to the host microorganism, and used to cause transcription/translation to proteins in this microorganism. The DNA introduced to this microorganism is preferably in the form incorporated in a vector. In other words, each gene is incorporated into an expression vector that can be expressed by the host cell, and this is introduced to the host cell.
The vector is not particularly limited so long as being autonomously replicable in the host cell, and retaining the AAT gene and/or ACD gene, and it is possible to use vectors suited to the respective microorganisms. As the vector for introducing DNA to microorganism belonging to Rhodococcus sp., for example, it is possible to use well-known vectors such as pK1, pK2, pK3 and pK4, as well as pSJ034 (refer to Japanese Unexamined Patent Application, Publication No. H10-337185), pSJ023 and pSJ002 (refer to Japanese Unexamined Patent Application, Publication No. H10-24867), and pSJ201 and pLK005 (not limited to these). pSJ023 is deposited in the National Institute of Advanced Industrial Science and Technology, Patent Organism Depository as transformant Rhodococcus rhodochrous ATCC12674/pSJ023 (FERMBP-6232).
The insertion of the above-mentioned AAT gene and/or ACD gene to the vector can be carried out using gene recombination technology known to those skilled in the art. For example, it is possible to utilize a method using restriction enzyme cleavage and ligation, a method using topoisomerase, an In Fusion kit (Takara Bio), and the like. The gene inserted into the vector is inserted successively downstream of a promotor capable of regulating transcription/translation of proteins encoded by the respective genes in the host organism. In addition, if necessary, an appropriate linker may be added upon insertion. In addition, as necessary, a terminator sequence, enhancer sequence, splicing signal sequence, polyA addition signal sequence, ribosome-binding sequence such as the SD sequence or Kozak sequence, selection marker gene, etc. usable in the host organism into which genes are trying to be introduced can be linked. As an example of the selection marker gene, in addition to drug resistant genes such as ampicillin-resistant gene, tetracycline-resistant gene, neomycin-resistant gene, kanamycin-resistant gene and chloramphenicol-resistant gene, genes imparting intracellular biosynthesis of nutrients such as amino acids and nucleic acids, or genes coding fluorescent proteins such as luciferase can be exemplified. Accompanying insertion, a part of the amino acid sequence coded by the DNA may be substituted.
From the above point, it is particularly preferable to use pLK005 acquired by performing variation treatment on pK4 as the vector. The AAT gene or ACD gene is linked/inserted so as to be disposed downstream of 3′ of the promoter of pLK005, and an expression plasmid vector that expresses AAT gene and/or ACD gene can be constructed by the promoter.
In the vector, any gene selected from the AAT gene cluster or ACD gene cluster may be inserted, and a plurality of genes may be inserted. In the case of a gene inserted in a vector being used, “plurality” can be inserting 2 to 5, 2 to 4, and preferably 2 or 3 genes. In addition, in the case of a plurality of genes being inserted into one vector, these genes preferably form an operon. Herein, “operon” is a nucleic acid sequence unit constituted from one or more genes transcribed under the control of the same promoter.
The above-mentioned genes, and preferably genes in the form of a vector, are inserted to the host microorganism by a method known to those skilled in the art. The introduction method of the recombinant vector to the host organism is not particularly limited so long as being a method suited to the host microorganism and, for example, the electroporation method, spheroplast method, lithium acetate method, calcium phosphate method, lipofection method, conjugational transfer method and the like can be exemplified.
Method for Producing Methacrylic Acid Ester
The recombinant microorganism to which the required genes such as AAT gene and/or ACD gene are introduced is brought into contact with the precursor to produce methacrylic acid ester. Herein, “contact” indicates exposure treating for a fixed time the microorganism and a substance (precursor). More specifically, the microorganism is cultured in an aqueous medium containing precursor (raw material), etc., or a culture of the microorganism is added to the aqueous medium containing raw material, and suspended/mixed, to obtain methacrylic acid ester in the aqueous medium and/or gas phase. Upon doing so, it is of no concern if there is proliferation of microorganism. In this process, a mixture containing recombinant microorganism, and methacrylic acid ester is obtained.
“Aqueous medium” indicates water or an aqueous solution with water as a principle component, and also includes those in which undissolved liquid/solid are dispersed. “Gas phase” refers to a portion occupied by gas, steam, etc. excluding a portion occupied by liquid (culture medium, etc.) in the culture tank (vessel culturing microorganism) or reactor (vessel carrying out reaction). “Culture” indicates that obtained by way of a culturing of bacterial cells, broth, noncellular extract, cellular membrane, or the like.
(1) Production of Methacrylic Acid Ester from Culturing
In the present invention, production of methacrylic acid ester is performed by causing methacrylic acid ester to be form and accumulate in culture bacterial cells or the culture by culturing gene recombinant microorganism to which AAT gene has been introduced in an aqueous medium containing the precursor, and recovering the methacrylic acid ester from the culture bacterial cell, culture or culture vessel gas phase.
The culture medium used in the culturing of microorganism is a solid medium or liquid medium enabling sufficient proliferation that contains nutrients at least including various carbon sources. In the case of precursor being usable as the carbon source, it can be used as the carbon source.
The concentration of carbon source or precursor in the culture medium is not particularly limited so long as enabling the production of methacrylic acid ester. The concentration, for example, is set to 0.05 to 20 (w/v) %, preferably 0.1 to 15 (w/v) %, and more preferably 0.2 to 10 (w/v) %. At least 0.2 (w/v) % is used because the methacrylic acid productivity of microorganisms increases, and it is set to no more than 10 (w/v) % because a dramatic improvement in effect is not recognized even if increasing to more than this.
In the production of methacrylic acid ester by culturing, alcohol or phenol is added depending on the target methacrylic acid ester. The alcohol or phenol used is preferably one shown by Formula 2.
The concentration of alcohol or phenol in the culture medium is not particularly limited so long as enabling methacrylic acid ester to be produced. The concentration, for example, is set to 0.01 to 20 (w/v) %, preferably 0.05 to 10 (w/v) %, and more preferably 0.1 to 5 (w/v) %. In addition, these can also be added to the culture medium in advance, or can be added continuously or intermittently by dividing into two or more occurrences, while performing culturing.
In the culture medium, inorganic nitrogen sources, inorganic metal salts or the like may be added. As inorganic nitrogen sources, for example, inorganic acids or organic acids of ammonium salts such as ammonium chloride, ammonium sulfate, ammonium acetate and ammonium phosphate, and the like can be used.
The concentration of nitrogen source in the culture medium is not particularly limited so long as enabling methacrylic acid ester to be produced. The concentration, for example, is set to 0.01 to 10 (w/v) %, preferably 0.05 to 8 (w/v) %, and more preferably 0.1 to 4 (w/v) %.
As inorganic metal salts, for example, potassium dihydrogen phosphate, potassium monophosphate, magnesium phosphate, magnesium sulfate, sodium chloride, ferrous sulfate, manganese sulfate, copper sulfate, calcium carbonate, etc. can be used.
The concentration of inorganic salts in the culture medium is not particularly limited so long as enabling methacrylic acid ester to be produced. The concentration, for example, is set to 0.001 to 1.6 (w/v) %, preferably 0.005 to 1.3 (w/v) %, and more preferably 0.01 to 1 (w/v) %. At least 0.1 (w/v) % is used because the methacrylic acid productivity of microorganisms increases, and it is set to no more than 1 (w/v) % because a dramatic improvement in effect is not recognized even if adding more than this.
Additionally, trace metals, vitamins, etc. are added as necessary to the culture medium. In addition, various organic substances, inorganic substances, surfactant, commonly used defoaming agent, etc. necessary in the breeding of the microorganism can be additionally added to the culture medium as necessary.
Seeding of the genetically modified microorganism to the culture medium may be carried out by a conventional, known technique. The culture method also is not particularly limited, and it is possible to use a known technique such as shaking culture, aerated and agitated culture, and static culture.
The culturing conditions are not particularly limited so long as the genetically modified organism breeds and forms methacrylic acid ester. Culturing may be carried out under aerobic conditions or may be carried out under anaerobic conditions.
The pH, temperature and culturing time are not particularly limited so long as conditions allowing the genetically modified microorganism to breed and form methacrylic acid ester. The pH is preferably set to 3 to 10, more preferably 4 to 9, and even more preferably 5 to 8. The temperature is preferably set to 10 to 45° C., more preferably 15 to 40° C., and even more preferably 20 to 35° C. The culturing time is preferably 10 to 1000 hours, more preferably 15 to 480 hours, and even more preferably 20 to 240 hours.
These culturing conditions are appropriately selected or optimized for every strain so as to maximize the ratio of yield of methacrylic acid ester relative to the utilized amount of carbon source or precursor. It should be noted that the yield of methacrylic acid ester can be adjusted by appropriately adjusting the amount of carbon source and culturing conditions.
As ideal conditions for causing methacrylic acid ester to accumulate in at least 0.001 mM, under a pH condition of 5.5 to 7.5, the concentration of carbon source or precursor in the culture medium is directly or indirectly maintained to at least 0.1%, the concentration of alcohol or phenols is directly or indirectly maintained to at least 0.1%, the temperature is adjusted to the range of 20 to 40° C., and allowed to react for at least 3 hours. Furthermore, it is preferable in order to obtain efficient productivity to maintain a state in which the concentration of microorganism in the culture solution is high in a range in which the environment of the culture solution does not become inappropriate for proliferation of the microorganism or cultured cells and the ratio of cells dying does not rise and, for example, by maintaining in at least 2 g/L as a dry weight, favorable production efficiency is obtained, and the accumulation concentration of production can be raised.
(2) Production of Methacrylic Acid Ester from Resting Microorganism Reaction
With the method for producing methacrylic acid ester according to the present invention, the following method can be employed in addition to the method by culturing genetically modified microorganism as described above. The genetically modified microorganism does not need to have reproductive activity, and a precultured culture can be brought into contact with an aqueous medium containing precursor to produce methacrylic acid ester by resting microorganism reaction unaccompanied by substantial proliferation.
The concentration of the precursor used in resting microorganism reaction may be the same as the above-mentioned case of production of methacrylic acid ester from culturing. The alcohol or phenol used in resting microorganism reaction and the concentration thereof may be the same as the above-mentioned case of production of methacrylic acid ester by culturing.
Inorganic metal salts, etc. may be added to the reaction solution. As inorganic metal salts, for example, potassium dihydrogen phosphate, potassium monophosphate, magnesium phosphate, magnesium sulfate, sodium chloride, ferrous sulfate, manganese sulfate, copper sulfate, calcium carbonate, etc. can be used.
The concentration of inorganic salts in the reaction solution is not particularly limited so long as enabling methacrylic acid ester to be produced. The concentration, for example, is set to 0.0001 to 2 (w/v) %, preferably 0.0003 to 1.3 (w/v) %, and more preferably 0.001 to 1 (w/v) %.
Additionally, trace metals, vitamins, etc. are added as necessary to the reaction solution. In addition, various organic substances, inorganic substances, surfactant, commonly used defoaming agent, etc. necessary in the reaction can be additionally added to the reaction solution as necessary.
In resting microorganism reaction, the culture solution of precultured genetically modified microorganism is used as is, or bacterial cells recovered by filtering, centrifuging or the like are used. The recovered culture is resuspended in an appropriate buffer solution or the like, and can be used by establishing in any bacteria concentration. For the buffer solution or the like, a normal saline solution, potassium phosphate buffer solution, tris-hydrochloric acid buffer solution, glycine-sodium hydroxide buffer solution, boric acid-sodium hydroxide buffer solution, or the like is used.
In addition, in the resting microorganism reaction, the processed product of the recovered culture (e.g., homogenate, crude enzyme, purified enzyme, etc.) can also be used. Furthermore, it may be fixed to an appropriate carrier by a known method, and this fixation product may be used in reaction.
The reaction conditions are not particularly limited so long as forming methacrylic acid ester. The reaction may be carried out under aerobic conditions or may be carried out under anaerobic conditions. The reaction method is also not particularly limited, and a well-known technique such as shaking reaction, aerated and agitated reaction, and static reaction can be used.
The pH, temperature and reaction time are not particularly limited so long as conditions that can form methacrylic acid ester. The pH is preferably set to 3 to 10, more preferably 4 to 9, and even more preferably 5 to 8. The temperature is preferably set to 10 to 45° C., more preferably 15 to 40° C., and even more preferably 20 to 35° C. The reaction time is preferably 5 to 180 hours, more preferably 10 to 150 hours, and even more preferably 15 to 120 hours.
These reaction conditions are appropriately selected or optimized for every strain so as to maximize the ratio of yield of methacrylic acid ester. It should be noted that the yield of methacrylic acid ester can be adjusted by appropriately adjusting the reaction conditions.
As ideal conditions for causing methacrylic acid ester to accumulate in 0.001 mM, under a pH condition of 5.5 to 7.5, the concentration of carbon source or precursor in the culture medium is directly or indirectly maintained to at least 0.1%, the concentration of alcohol or phenols is directly or indirectly maintained to at least 0.1%, the temperature is adjusted to the range of 20 to 40° C., and allowed to react for at least 3 hours. Furthermore, maintaining a state in which the concentration of microorganism in the reaction solution is high is preferable to obtain efficient productivity, and for example, by maintaining in at least 2 g/L as a dry weight, favorable production efficiency is obtained, and the accumulation concentration of product can be improved.
In the method for producing methacrylic acid ester according to the present invention, the aforementioned production of methacrylic acid ester from culturing and the production of methacrylic acid ester from resting microorganism reaction may be carried out by combining as appropriate. By combining the two methods, the more efficient production of methacrylic acid ester becomes possible.
(3) Recovery of Methacrylic Acid Ester
The methacrylic acid ester formed in the culture medium or reaction solution and the formed amount thereof can be detected and measured using a common method such as of high-performance liquid chromatography and LC-MS. In addition, the methacrylic acid ester volatilized in the gas phase of the culture container or reaction container (head space part) and formed amount thereof can be detected and measured using a common method such as gas chromatography.
The methacrylic acid ester can be separated and purified from the culture medium or reaction solution using an appropriate combination, as necessary, of well-known operations such as filtration, centrifugation, vacuum concentration, ion exchange or adsorption chromatography, solvent extraction, distillation and crystallization.
EXAMPLES
Hereinafter, although the present invention will be specifically explained by way of Examples; however, the scope of the present invention is not to be limited to the scope of these examples.
Example 1: Synthesis of Isobutyl Methacrylate
The skin of a banana was removed, the sarcocarp was sliced to about 1 millimeter thickness with a cutter, and this was further divided into four. Two grams of sliced banana, 2 ml of a solution containing 2.3 mM methacrylyl-CoA and 0.35 M of KCl and 5 μl of isobutyl alcohol were added in order to a 100 ml flask. It was sealed and allowed to react at 30° C. The reaction mixture containing Isobutyl methacrylate formed after 1, 2 or 3 hours was collected in a 100 ml flask with 150 μl of head space, and analysis was performed with the GC conditions below. The results thereof are shown in Table 1.
TABLE 1
Generated amount of isobutyl methacrylate
Time Generated amount of isobutyl methacrylate (mM)
1 0.19
2 0.38
3 0.45

GC Analysis Conditions
column: DB-WAX, 30 m×0.32 mm
column temperature: 50° C.·5 min→5° C./min→100° C. (15 min total)
carrier gas: He
inject: 200° C. splitless (sampling time 1 min)
detect: 250° C. FID
injection volume: 150 μl
It should be noted that the concentration of methacrylic acid ester was calculated by adjusting an aqueous solution of a known initial concentration, placing 2 ml of the same aqueous solution in a 100 ml flask, and after incubating for 30 min at 30° C., collecting the head space by the same method, subjecting to GC analysis, and preparing a calibration curve.
Example 2: Synthesis of Butyl Methacrylate
Except for using n-butyl alcohol in place of isobutyl alcohol, it was conducted similarly to Example 1. The results thereof are shown in Table 2.
TABLE 2
Generated amount of butyl methacrylate
Time Generated amount of butyl methacrylate (mM)
2 0.20
5.5 0.30
Example 3: Synthesis 2 of Butyl Methacrylate
Two grams of a plant piece shown in Table 3, 2 ml of a solution containing 2.3 mM of methacrylyl-CoA and 0.35 M KCl and 10 μl of n-butyl alcohol were added in order to a 100 ml flask. It was sealed and allowed to react at 30° C. Analysis of the methacrylic acid ester was conducted similarly to Example 1. The results thereof are shown in Table 3.
TABLE 3
Generated amount of butyl methacrylate
Generated
amount of
butyl
Reaction methacrylate
Plant Part used time (mM)
Strawberry Sliced sacrocarp to about 3 0.010
1 mil thickness
Kiwi Sliced sacrocarp to about 5 0.012
1 mil thickness
Apple Sliced pericarp to about 5 0.016
1 mil thickness
Melon Sliced sacrocarp to about 6 0.015
1 mil thickness
Pear Sliced pericarp to about 4 0.013
1 mil thickness
Papaya Sliced pericarp to about 4 0.027
1 mil thickness
Avocado Sliced pericarp to about 6 0.035
1 mil thickness
Blueberry Sliced pericarp to about 6 0.009
1 mil thickness
Prunus mume Sliced pericarp to about 4 0.002
1 mil thickness
Example 4: Synthesis of Ethyl Methacrylate
Two grams of plant piece shown in Table 4, 2 ml of a solution containing 2.3 mM of methacrylyl-CoA and 0.35 M KCl and 6.4 μl of ethyl alcohol were added in order to 100 ml flask. It was sealed and allowed to react at 30° C. Analysis of the methacrylic acid ester was conducted similarly to Example 1. The results thereof are shown in Table 4.
TABLE 4
Generated amount of ethyl methacrylate
Generated amount of
Reaction ethyl methacrylate
Plant Part used time (mM)
Apple Sliced pericarp to 5 0.110
about 1 mil thickness
Papaya Sliced pericarp to 6 0.003
about 1 mil thickness
Avocado Sliced pericarp to 6 0.006
about 1 mil 6 thickness
Example 5: Synthesis of Ethyl Methacrylate
Two grams of a plant piece shown in Table 5, 2 ml of a solution containing 2.3 mM of methacrylyl-CoA and 0.35 M KCl and 4.4 μl of methyl alcohol were added in order to a 100 ml flask. It was sealed and allowed to react at 30° C. Analysis of the methacrylic acid ester was conducted similarly to Example 1. The results thereof are shown in Table 5.
TABLE 5
Generated amount of methyl methacrylate
Generated amount of
Reaction ethyl methacrylate
Plant Part used time (mM)
Apple Sliced pericarp to 5 0.043
about 1 mil thickness
Papaya Sliced pericarp to 6 0.004
about 1 mil thickness
Avocado Sliced pericarp to 6 0.007
about 1 mil 6 thickness
Reference Example 1: Preparation of Competent Cell
E. coli JM109 was innoculated in 1 mL of LB medium (1% Bacto tryptone, 0.5% Bacto yeast extract, 0.5% NaCl), precultured aerobically at 37° C. for 5 hours, 0.4 mL of the culture was added to 40 mL of SOB medium (2% Bacto tryptone, 0.5% Bacto yeast extract, 10 mM NaCl, 2.5 mM KCl, 1 mM MgSO4, 1 mM MgCl2), and was cultured at 18° C. for 20 hours. After harvesting this culture by centrifugation, 13 mL of a chilled TF solution (20 mM PIPES-KOH (pH 6.0), 200 mM KCl, 10 mM CaCl2, 40 mM MnCl2) was added, and left to stand for 10 minutes at 0° C. Subsequently, after re-centrifuging to remove supernatant, the precipitated E. coli was suspended in 3.2 mL of cold TF solution, 0.22 mL of dimethylsulfoxide was added thereto, and left to stand for 10 minute at 0° C. to prepare a competent cell.
Example 6: Preparation of Plant-Derived AAT Gene-Introduced Recombinant E. coli
The plant-derived AAT genes shown in SEQ ID NOS: 2, 4 and 6 were entrusted for synthesis by Takara Bio Inc. Apple AAT
(MpAAT1): amino acid sequence (SEQ ID NO: 1), nucleotide sequence (SEQ ID NO: 2)
Strawberry AAT (SAAT): amino acid sequence (SEQ ID NO: 3), nucleotide sequence (SEQ ID NO: 4)
Strawberry AAT (VAAT): amino acid sequence (SEQ ID NO: 5), nucleotide sequence (SEQ ID NO: 6)
These synthesized gene segments were inserted in vector pMD19, and respectively named pAAT001 to 003. (Table 6) With these pAAT001 to 003 as templates, DNA fragments coding AAT gene were prepared by way of the PCR method, designing an oligonucleotide so as to be a form in which a restriction endonuclease recognition site enabling easy introduction to an expression vector was added.
Oligonucleotide Primer
(SEQ ID NO. 11)
MMA-044: 5′-GTTTGCACGCCTGCCGTTCGACG-3′
(SEQ ID NO. 12)
MMA-045: 5′-CGGTACGCGCGGATCTTCCAGAG-3′

Reaction Solution Composition
Sterilized water 22 μL
2× PrimeSTAR (manufactured by Takara Bio) 25 μL
Forward primer 1 μL
Reverse primer 1 μL
Genomic DNA 1 μL
Total amount 50 μL
Temperature Cycle
30 cycles of reaction at 98° C. 10 seconds, 55° C. 15 seconds and 72° C. 150 seconds
A band of obtained amplification product was purified by a QIAquick Gel Extraction Kit (QIAGEN). The respective purified DNA was digested with restriction enzyme PagI (cleavage recognition site included in Forward Primer) and Sse8387I (cleavage recognition site included in Reverse Primer). Separation was performed by agarose gel electrophoresis, the target band was excised from the gel, and purification was performed. In purification, using a Gel/PCR Purification Kit (manufactured by FAVORGEN), it was eluted to 30 μL of sterile water.
The purified DNA (5 μL), vector pTrc99A digested with NcoI and Sse8387I (1 μL), distilled water (4 μL) and solution I (DNA Ligation Kit ver. 2 (Takara Bio)) (10 μL) were mixed, and the vector was ligated with PCR amplification product by incubating for 12 hours at 16° C.
To 200 μL of the compenent cell prepared by the method of Reference Example 1, 10 μL of the above-mentioned ligation solution was added and left to stand at 0° C. for 30 minutes, followed by imparting heat shock at 42° C. for 30 seconds and cooling to 0° C. for 2 minutes, after which 1 mL of SOC culture medium (20 mM glucose, 2% Bacto tryptone, 0.5% Bacto yeast extract, 10 mM NaCl, 2.5 mM KCl, 1 mM MgSO4, 1 mM MgCl2) was added and shaking cultured at 37° C. for 1 hour.
After culturing, 100 μL of culture media was inoculated to LBAmp nutrient agar (LB culture medium containing 100 mg/L ampicillin, 1.5% agar), and further cultured at 37° C. A plurality of transformant colonies grown on nutrient agar was cultured overnight at 37° C. in 1.5 mL of LBAmp culture medium (LB culture medium containing 100 mg/L ampicillin), and after harvesting, plasmid DNA was prepared using a QIAprep Spin Miniprep kit (QIAGEN).
For the obtained recombinant respective plasmid DNA, the nucleotide sequence thereof was confirmed using a CEQ DTCS Quick Start Kit and fluorescent sequencer CEQ 2000XL DNA Analyzer (both Beckman Coulter, USA), and were named plasmid pAAT101 to pAAT103 (Table 6).
For the pET16b vectors, AAT gene was introduced by similar operations, and the obtained plasmids were named pAAT201 to pAAT203 (Table 6). However, since there is no Sse8387I site in pET16b, that in which a linker including the Sse8387I cleavage sequence had been inserted at the BamHI site of pET16b was prepared in advance, and this was used as a vector.
The plasmids pAAT101 to pAAT103 were introduced to JM109 strain to obtain recombinant JM109/pAAT101 to pAAT103. The plasmids pAAT201 to pAAT203 were introduced to the BL21(DE3) strain to obtain recombinant BL21(DE3)/pAAT201 to pAAT203.
TABLE 6
Plasmid for plant-derived AAT gene expression
Plant origin Template Expression plasmid
SEQ ID NO (gene name) plasmid pTrc99A pET16b
2 Apple (MpAAT1) pAAT001 pAAT101 pAAT201
4 Strawberry (SAAT) pAAT002 pAAT102 pAAT202
6 Strawberry (VAAT) pAAT003 pAAT103 pAAT203
Example 7: Preparation of Cell-Free Extract from Recombinant E. coli Expressing AAT Gene
(1) Culturing of Recombinant E. coli Using pTrc99A as Vector
The Recombinant E. colis JM109/pAAT101 to pAAT103 obtained in Example 6 were inoculated into 1 ml of an LB culture medium containing 100 μg/ml of ampicillin, and preculturing was performed at 37° C. for 7 hours. The broth was taken in 0.1 ml, added to 100 ml of the same culture medium (100 μg/ml ampicillin, 1 m MIPTG contained), and shaking cultured at 37° C. for 15 hours. The bacterial cell was recovered by way of centrifugation (3,700×g, 10 min, 4° C.) from the obtained broth, and after washing with a 10 mM sodium phosphate buffer solution (pH 7.0), was suspended in the same buffer solution. JM109/pTrc99A was used as a reference strain.
(2) Culturing of Recombinant E. coli Using pET16b as Vector
The recombinant E. colis BL21(DE3)/pAAT201 to pAAT203 obtained in Example 6 were inoculated into 1 ml of an LB culture medium containing 100 μg/ml of ampicillin, and preculturing was performed at 37° C. for 14 hours. The broth was taken in 0.1 ml, added to 100 ml of the same culture medium (100 μg/ml ampicillin), and after shaking cultured at 37° C. until the OD became 0.3, IPTG was added so that the final concentration became 1 mM and was further shaking cultured for several hours. The bacterial cell was recovered by way of centrifugation (3,700×g, 10 min, 4° C.) from the obtained broth, and after washing with a 10 mM sodium phosphate buffer solution (pH 7.0), was suspended so as to be OD=6 (630 nm) in the same buffer solution. BL21(DE3)/pET16b was used as a reference strain.
(3) Preparation of Cell-Free Extract
Cell-free extract was prepared from the obtained bacterial cell suspension. Using an ultrasonic homogenizer VP-15S (Taitec, Japan), homogenizing was performed for 1 minute while keeping the bacterial cell suspension on ice at conditions of output control 4, DUTY CYCLE 40%, PULS, TIMER=B mode 10 s. Next, centrifugation was performed (10,000×g, 5 minutes, 4° C.), and 1 ml of the obtained supernatant (cell-free extract) was collected.
Example 8: Synthesis of Butyl Methacrylate Using AAT Gene Recombinant Cell-Free Extract
The following reaction was performed using cell-free extract prepared by the method described in Example 7. The reaction was initiated by adding 0.2 ml of cell-free extract to a 10 ml-sample bottle with a septum (for GC) into which 0.8 ml of a solution of methacrylyl-CoA and alcohol was placed so that the final concentration of the reaction solution was 7 mM methacrylyl-CoA and 40.5 mM n-butanol. The sample bottle with a septum was incubated at 30° C. for 1 to 5 hours to cause reaction.
The gas in the head space of the sample bottle with a septum was analyzed similarly to Example 1. The results are shown in Table 7.
TABLE 7
Formation of butyl methacrylate using AAT gene recombinant
Generated amount (mM)
Recombinant 1 hour 3 hours 5 hours
JM109/pAAT102 0.001 0.003 0.004
JM109/pAAT103 0 0.001 0.002
BL21(DE3)/pAAT201 0.003 0.014 0.026
BL21(DE3)/pET6b 0 0 0
Example 9A: Synthesis of Methacrylic Acid Ester Using AAT Gene Recombinant Cell-Free Extract
The reaction was carried out similarly to Example 8 using methanol, ethanol or n-butanol as the alcohol, and using that derived from BL21(DE3)/pAAT201 (apple) in the cell-free extract. The analysis results of the product after 5 hours are shown in Table 8.
TABLE 8
Generation of methacrylic acid ester using AAT gene recombinant
Generated amount after 5 hours (mM)
Ethyl Butyl
Recombinant Methyl methacrylate methacrylate methacrylate
BL21(DE3)/pAAT201 0.021 0.045 0.091
Example 9B: Synthesis 2 of Methacrylic Acid Ester Using AAT Gene Recombinant Cell-Free Extract
Using isobutanol, butanol, benzyl alcohol or 2-ethylhexyl alcohol, the following reaction was carried out with the cell-free extract of BL21(DE3)/pAAT201 (apple) obtained in Example 7.
The reaction was initiated by adding 0.2 ml of cell-free extract to a 10 ml-sample bottle with a septum (for GC) into which 0.8 ml of a solution containing methacrylyl-CoA and alcohol was placed so that the final concentration of the reaction solution was 1 mM methacrylyl-CoA and 40 mM n-butanol.
The sample bottle with a septum was incubated at 30° C. for 1 to 5 hours to cause reaction. After reaction completion, 1 mL of acetonitrile was added and mixed to the reaction solution in the sample bottle with a septum. Subsequently, after filtration using a syringe filter DISMIC/pore size 0.45 μm (manufactured by ADVANTEC), it was provided for HPLC analysis. The analysis results of the product after 5 hours are shown in Table 9.
Synthesis of Methacrylic Acid Esters (Isobutyl Methacrylate, Phenyl Methacrylate, Benzyl Methacrylate, 2-Ethylhexyl Methacrylate) Using AAT Gene Recombinant
TABLE 9
Generated amount after 5 hours (mM)
Isobutyl Phenyl Benzyl 2-ethylhexyl
Recombinant methacrylate methacrylate methacrylate methacrylate
BL21(DE3)/ 0.009 0.001 0.17 0.31
pAAT201

HPLC Analysis Conditions
Device: Waters 2695
Column: Shiseido CAPCELL PAK C18 UG120 5 μm
Mobile phase: 65% MeOH, 0.2% phosphoric acid
Flow rate: 0.25 ml/min
Column temperature: 35° C.
Detection: UV 210 nm
Injection volume: 10 μL
Example 10: Preparation of Recombinant E. coli Introduced with ACD Gene
Preparation of High-Expression Recombinant with Cloning of ACD Homolog Gene from Pseudomonas aeruginosa PAO1
(1) Preparation of Genomic DNA from Pseudomonas aeruginosa PAO1
Pseudomonas aeruginosa PAO1 strain (NBRC106052) grown on LB nutrient agar (1% Bacto tryptone, 0.5% Bacto yeast extract, 0.5% NaCl, 1.5% agar) was inoculated to 10 ml of LB liquid culture medium (1% Bacto tryptone, 0.5% Bacto yeast extract, 0.5% NaCl), and shaking culturing was performed at 37° C. for 15 hours. After culturing completion, the bacterial cell was recovered by way of centrifuge from 2 ml of the broth, and 100 μl of genomic DNA was prepared using a Wizard Genomic DNA Purification Kit (Promega KK).
(2) Cloning of Expression Vector
The obtained genomic DNA was made a template, and a DNA fragment including a gene assumed to code ACD was prepared by way of the PCR method so as to be a form in which a restriction endonuclease recognition site enabling easy introduction to an expression vector was added.
Oligonucleotide Primer
(SEQ ID NO. 13)
MMA-003: 5′-GACCCATGGATTTCGACCTCACCGAAGAAC-3′
(SEQ ID NO. 14)
MMA-004: 5′-GCCCTGCAGGATGCGATGGTTCGCGGCGTTC-3′

Reaction Solution Composition
Sterilized water 22 μl
2× PrimeSTAR (manufactured by Takara Bio) 25 μl
MMA-003 (SEQ ID NO. 13) 1 μl
MMA-004 (SEQ ID NO. 14) 1 μl
Genomic DNA 1 μl
Total amount 50 μl
Temperature Cycle
30 cycles of reaction at 98° C. 10 seconds, 55° C. 15 seconds and 72° C. 150 seconds
A band of about 1.2 kb of the obtained amplification product was purified by a QIAquick Gel Extraction Kit (QIAGEN). The purified DNA was digested with digested with restriction enzyme NcoI (cleavage recognition site included in oligonucleotide MMA-003) and Sse8387I (cleavage recognition site included in oligonucleotide MMA-004), and purified by way of phenol extraction/chloroform extraction/ethanol precipitation. The purified DNA (5 μL), vector pTrc99A digested with NcoI and Sse8387I (1 μL), distilled water (4 μL) and solution I (DNA ligation Kit ver. 2 (Takara Bio)) (10 μL) were mixed, and the vector was ligated with PCR amplification product by incubating for 12 hours at 16° C.
To 200 μL of the competent cell prepared by the method of Reference Example 1, 10 μL of the above-mentioned ligation solution was added and left to stand at 0° C. for 30 minutes, followed by imparting heat shock at 42° C. for 30 seconds and cooling to 0° C. for 2 minutes, after which 1 mL of SOC culture medium (20 mM glucose, 2% Bacto tryptone, 0.5% Bacto yeast extract, 10 mM NaCl, 2.5 mM KCl, 1 mM MgSO4, 1 mM MgCl2) was added and shaking cultured at 37° C. for 1 hour.
After culturing, 200 μl of culture media was inoculated to LBAmp nutrient agar (LB culture medium containing 100 mg/L ampicillin, 1.5% agar), and further cultured at 37° C. A plurality of transgenic organism colonies cultured on nutrient agar was cultured overnight at 37° C. in 1.5 mL of LBAmp culture medium (LB culture medium containing 100 mg/L ampicillin), and after harvesting, plasmid DNA was recovered using a Flexi Prep (manufactured by Amersham Biosciences).
(3) Transformation
For the obtained recombinant plasmid DNA, the nucleotide sequence thereof was confirmed using a CEQ DTCS Quick Start Kit and fluorescent sequencer CEQ 2000XL DNA Analyzer (both Beckman Coulter, USA), and was named plasmid pMMA002. The E. coli JM109 strain was transformed using the plasmid pMMA002 to prepare a recombinant to which the ACD gene (SEQ ID NO. 8) had been introduced. The amino acid sequence is shown by SEQ ID NO. 7.
Example 11: Preparation of Cell-Free Extract from Recombinant E. coli Expressing ACD Gene
Recombinant E. coli JM109/pMMA002 to which the ACD gene (SEQ ID NO. 8) obtained in Example 10 had been introduced was inoculated to 1 ml of an LB culture medium containing 100 μg/ml ampicillin, and preculturing was performed at 37° C. for 7 hours. The broth was taken in 0.1 ml, added to 100 ml of the same culture medium (100 μg/ml ampicillin, 1 m MIPTG contained), and shaking cultured at 37° C. for 15 hours. The bacterial cell was recovered by way of centrifugation (3,700×g, 10 min, 4° C.) from the obtained broth, and after washing with a 10 mM sodium phosphate buffer solution (pH 7.0), was suspended so as to be OD=6 (630 nm) in the same buffer solution. JM109/pTrc99A was used as a reference strain.
From the obtained bacterial cell suspension, 1 ml of cell-free extract was prepared as follows. Using an ultrasonic homogenizer VP-15S (Taitec, Japan), homogenizing was performed for 1 minute while keeping on ice at conditions of output control 4, DUTY CYCLE 40%, PULS TIMER=B mode 10 s. Next, centrifugation was performed (10,000×g, 5 minutes, 4° C.), and the obtained supernatant was collected as cell-free extract.
Example 12: Preparation of Butyl Methacrylate from Isobutyryl-CoA Using Plant Fragment and ACD Genetically Modified Recombinant Cell-Free Extract
(1) Methacrylyl-CoA Synthesis Reaction with Isbutyryl-CoA as Substrate by ACD Genetically Modified Recombinant Cell-Free Extract
To 1.84 ml of a solution containing 6 mM 1-methoxy-5-methyl phenazinium metilsulfate, 0.4 mM flavin adenine dinucleotide and 1 mM isobutyryl-CoA in a 100 mM sodium phosphate buffer solution (pH 8.0), 0.16 ml of cell-free extract having ACD activity obtained in Example 10 was added to prepare 2 ml of reaction solution. It was allowed to react at 37° C. for 30 minutes, and analysis was performed at the HPLC conditions shown below. As a result thereof, the peak of isobutyryl-CoA disappeared, thereby confirming the formation of methacrylyl-CoA.
HPLC Analysis Conditions
Column: Inertsil ODS-3V, 4.6 mm×250 mm
Mobile phase: 30% MeOH, 50 mM H3PO4, pH 5.7
Flow rate: 1.0 ml/min
Column temperature: 35° C.
Detection: UV 254 nm
Injection volume: 10 μl
Reaction solution diluted 10 times with mobile phase and measured.
(2) Synthesis of Butyl Methacrylate by Addition of n-Butyl Alcohol and Plant Fragment to Methacrylyl-CoA Synthesis Reaction Solution
The skin of a banana was removed, the sarcrocarp was sliced with a cutter to a thickness of about 1 millimeter, and this was further divided into four. To a 50-ml flask, 1 g of the sliced banana, 0.9 ml of the methacrylyl-CoA synthesis reaction solution, 0.1 ml of 3.5 M KCl solution and 5 μl of n-butyl alcohol were added, sealed, and then allowed to react at 30° C. for 2 hours. Upon conducting analysis of methacrylic acid ester similarly to Example 1, 0.015 mM of butyl methacrylate formed.
Example 13: Preparation of Recombinant E. coli Introduced with ECH Gene
(1) Preparation of Genomic DNA from Rhodococcus Bacterium
Rhodococcus erythropolis PR4 strain (NBRC100887) grown on LB nutrient agar culture medium was inoculated to 10 mL of LB liquid culture medium, and shaking culturing was performed at 30° C. for 36 hours. After culturing completion, the bacterial cell was recovered by way of centrifuge from 2 ml of the broth, and 100 μl of genomic DNA was acquired similarly to Example 10.
(2) Cloning of Expression Vector
The obtained genomic DNA was made a template, and a DNA fragment including a nucleotide sequence assumed to encode ECH gene was prepared by way of the PCR method so as to be a form in which a restriction endonuclease recognition site enabling easy introduction to an expression vector is added.
Oligonucleotide Primer:
(SEQ ID NO. 15)
MMA-031: 5′-GGTCATGACCGACTTCAACACCATCATCCTC-3′
(SEQ ID NO. 16)
MMA-032: 5′-GGCCTGCAGGTTCAGCTGTTCGAAAGTTCAGCGC-3′
PCR was performed similarly to Example 10, and the obtained DNA was digested with restriction enzyme BspHI (cleavage recognition site included in oligonucleotide MMA-031) and Sse8387I (cleavage recognition site included in oligonucleotide MMA-032). After cleavage, the same operations as Example 6 were performed to acquire the target plasmid DNA to which ECH gene (SEQ ID NO. 10) was incorporated, and then named plasmid pMMA011. The amino acid sequence is shown by SEQ ID NO. 9.
(3) Transformation
E. coli JM109 strain was transformed using plasmid pMMA011 to prepare ECH gene expression Recombinant E. coli.
Example 14: Synthesis of Butyl Methacrylate from 3-Hydroxyisobutyryl-CoA Using ECH Gene Expression Recombinant E. coli Cell-Free Extract and AAT Gene Recombinant Cell-Free Extract
(1) Preparation of Cell-Disrupted Liquid Having ECH Activity
The Recombinant E. coli JM109/pMA011 to which the ECH gene obtained in Example 13 had been introduced was inoculated in an LB culture medium containing 2 ml of 100 μg/ml ampicillin, and preculturing was performed at 37° C. for 24 hours. The broth was taken in 0.1 ml, added to 100 ml of the same culture medium (100 μg/ml ampicillin, 1 m MIPTG contained), and shaking cultured at 37° C. for 15 hours. The bacterial cell was recovered by way of centrifugation (3,700×g, 10 min, 4° C.) from the obtained broth, and after washing twice with a 10 mM sodium phosphate buffer solution (pH 7.0), was diluted so as to be O=D6 (630 nm) in the same buffer solution.
From the obtained bacterial cell suspension, 1 ml of cell-disrupted liquid was prepared in the following way. Using an ultrasonic homogenizer Sonifier 250D (Branson, USA), it was homogenized for 5 minutes while keeping on ice at conditions of amplitude: 15%/On: 1 sec, off: 1 sec.
(2) Methacrylyl-CoA Synthesis Reaction Using ECH Gene Expression Recombinant E. coli Cell-Disrupted Liquid
To the mixture prepared by mixing 0.2 ml of 0.5 M tris-HCl buffer solution (pH 7.4), 0.4 ml of 1.2 mM 3-hydroxyisobutyryl-CoA aqueous solution and 1.2 ml of water, 0.2 ml of cell-disrupted liquid having enoyl-CoA hydratase activity obtained in the above way was added to prepare 2 ml of reaction solution. It was allowed to react at 37° C. for 30 minutes, and analysis was performed at the HPLC conditions shown in Example 12. As a result thereof, the formation of methacrylyl-CoA was confirmed.
(3) Synthesis of Butyl Methacrylate Using AAT Gene Recombinant Cell-Free Extract
To a 10-ml sample bottle, 0.4 ml of the methacrylyl-CoA synthesis reaction solution, 0.1 ml of 10 mM sodium phosphate buffer solution (pH 7.5) and 0.2 ml of water were added, 0.1 ml of 0.4 M n-butanol solution and 0.2 ml of apple AAT (MpAAT) cell-disrupted liquid prepared similarly to Example 7 were further added, sealed, and then allowed to react at 30° C. for 3 hours. Upon conducting analysis of methacrylic acid ester similarly to Example 1, 0.001 mM of Butyl methacrylate formed.
Example 15: Preparation of High-Expression Recombinant with Cloning of BCKAD Gene, Preparation of Cell-Free Extract, and Protein Expression Analysis
The preparation of expression plasmid with gene cloning and preparation of recombinant were performed similarly to Example 10. Genomic DNA of Pseudomonas aeruginosa PAO1 strain was made a template, and a DNA fragment including the entire gene operon coding BCKAD complex gene was prepared by way of the PCR method using the primer shown below. The obtained fragment was digested by restriction enzyme BspHI and Sse8387I, and inserted into vector pTrc99A similarly to Example 10 to obtain the recombinant plasmid (pWA108).
Oligonucleotide Primers:
(SEQ ID NO. 17)
MAA-15: 5′-GGCCTGTCATGAGTGATTACGAGCCG-3′
(SEQ ID NO. 18)
MAA-16: 5′-CGGCCCTGCAGGTTCGCGGGAATCAGATGTGC-3′
The Recombinant E. coli JM109/pWA108 obtained in the above way was cultured similarly to Example 10. However, in the case of the present recombinant, since high expression of protein was recognized even without performing addition of IPTG based on the preliminary results, it was conducted without the addition of IPTG. The preparation of cell-free extract was conducted similarly to Example 11.
Example 16: Activity Measurement of Cell-Free Extract of BCKAD Gene High-Expression Recombinant
The BCKAD activity was measured from the generation of isobutyryl-CoA with 2-oxoisovaleric acid as the substrate in the following way.
To 0.7 ml of a solution containing final concentrations of 1 mM MgCl2, 0.2 mM thiamin pyrophosphate, 1 mM CoA-Sh and 2 mM DDT in a 100 mM sodium phosphate buffer solution (pH 7.0), 0.2 ml of the cell-free extract obtained in Example 15 was added to make up 0.9 mL. After adding 0.1 mL (4 mM final concentration) of 2-oxoisovaleric acid calcium salt to this and reacting at 37° C. for 30 minutes, ultrafiltration was performed using a Centricut Super Mini W-10 (Kurabo Industries Ltd.). The reaction was stopped by performing deproteinization, and analysis was performed by HPLC at the following conditions. As a result thereof, the formation of 0.83 mM isobutyryl-CoA was recognized with JM109/pWA108.
HPLC Analysis Conditions
Column: Inertsil ODS-3V, 4.6 mm×250 mm
Mobile phase: 35 MeOH, 50 mM H3PO4, pH 5.7
Flow rate: 1.0 ml/min
Column temperature: 35° C.
Detection: UV254 nm (210 nm)
Injection volume: 10 μl (reaction solution diluted 10 times with mobile phase and measured)
Example 17: Synthesis of Methacrylyl-CoA (FIG. 1) from 2-Oxoisovaleric Acid by Cell-Free Extract Mixture from BCKAD Gene High-Expression Recombinant and Recombinant Expressing ACD Gene
To 0.6 ml of a solution containing final concentrations of 1 mM MgCl2, 0.2 mM thiamin pyrophosphate, 1 mM CoA-SH, 2 mM DDT, 2 mM nicotinamide adenine dinucleotide (NAD), 0.04 mM flavin adenine dinucleotide (FAD) and 2 mM valine in a 100 mM sodium phosphate buffer solution (pH 7.0), 0.1 ml of each of the cell-free extracts (JM109/pMMA002 and JM109/pWA108) obtained by the methods of Example 11 and Example 15 was respectively added to make up 0.8 mL. After adding 0.1 mL of 2-oxoisovaleric acid calcium salt (4 mM final concentration) to this and reacting at 37° C. for 30 minutes, the formation of isobutyryl-CoA was confirmed by HPLC, and 0.1 mL of 1-methoxy-5-methyl phenazinium metilsulfate (6 mM final concentration) was added and allowed to further react for 3 hours. After reaction, ultrafiltration was performed using a Centricut Super Mini W-10 (Kurabo Industries Ltd.). The reaction was stopped by performing deproteinization, and analysis was performed by HPLC. As a result thereof, the formation of 0.2 mM methacrylyl-CoA was recognized.
Reference Example 2: Preparation of Conjugational Transfer Recipient PR4KS
Rhodococcus erthropolis PR4 (NITE Biological Resource Center; deposit number: NBRC 100887) was modified by the method described in Japanese Unexamined Patent Application, Publication No. 2011-200133 to prepare a derivative exhibiting resistance to 120 mg/L chloramphenicol and lacking kanamycin-resistant gene, and was named as PR4KS strain.
More specifically, in order to enhance chloramphenicol resistance, the concentration of chloramphenicol in an MYK culture medium (0.5% polypeptone, 0.3% bact-yeast extract, 0.3% malt extract, 0.2% KH2PO4, 0.2% K2HPO4) was gradually raised step-wise starting from 10 mg/mL until 120 mg/mL, while inducing spontaneous mutation by subculturing PR4 strain, thereby obtaining derivative RhCmSR-09 strain having resistance to 120 mg/mL of chloramphenicol.
Next, the above-mentioned RhCmSR-09 strain was mixed at a 1:1 ratio with E. coli retaining the plasmid pKM043 for the kanamycin-resistant gene deficiency variation introduction described in Japanese Unexamined Patent Application, Publication No. 2011-200133, then cultured, and after introducing pKM043 into the RhCmSR-09 strain by conjugational transfer, was cultured in MYK nutrient agar containing 200 mg/L kanamycin sulfate and 50 mg/L chloramphenicol (0.5% polypeptone, 0.3% bact yeast extract, 0.3% malt extract, 0.2% KH2PO4, 0.2% K2HPO4, 1.5% agar), thereby obtaining a homologous recombinant strain in which pKM043 had been introduced into the RhCmSR-09 strain genome. The homologous recombinant strain was cultured in 10% sucrose-containing MYK nutrient agar, whereby a derivative strain emerging as a kanamycin-sensitive strain from among the obtained colonies, i.e. kanamycin-resistant gene deficiency variation derivative strain PR4KS, was obtained.
Reference Example 3: Preparation of Plasmid for Gene Deficiency with Cloning of LigD Homolog Gene
The LigD homolog gene (accession No: YP_002767969) of the PR4KS strain was established as the target gene. After amplification of about 5.4 kb of DNA including the LigD homolog gene surrounding sequence by way of PCR, it was cloned to plasmid vector pK19mobsacB1 to which the sacB gene had been introduced downstream and in the same orientation of the kanamycin-resistant gene, described in Japanese Unexamined Patent Application, Publication No. 2011-200133, thereby obtaining plasmid pTJ001. The PCR conditions were as follows.
Primers
(SEQ ID NO. 19)
GB-138: 5′-GGCCTGCAGGTACCGATCATCACCATCGGTGTC-3′
(SEQ ID NO. 20)
GB-139: 5′-GGTCTAGACTGAGCAGTGTTCCAATGCG-3′

Reaction Solution Composition
Sterilized water 22 μl
2× PrimeSTAR (manufactured by Takara Bio) 25 μl
GB-138 (SEQ ID NO. 19) 1 μl
GB-139 (SEQ ID NO. 20) 1 μl
PR4KS genome (50 ng/μL) 1 μl
Total amount 50 μl
Temperature Cycle
35 cycles of reaction at 98° C. 10 seconds, 55° C. 15 seconds and 72° C. 120 seconds
The plasmid for LigD homolog gene deficiency pTJ002 was prepared in which the entire length of the LigD homolog sequence inside pTJ001 (about 2.3 kb) was deleted and only the upstream and downstream sequences of the LigD homolog gene were allowed to remain (refer to FIG. 3). The sequence within pTJ001 was amplified using primers GB-140 and GB-141, which include the surrounding sequence of the start codon and the surrounding sequence of the stop codon of the targeted LigD homolog gene, respectively, and which were designed so as to extend in the upstream direction from the start codon and in the downstream direction of the stop codon, respectively, in order to obtain PCR product that does not include the LigD homolog gene. E. coli JM109 strain was transformed by the obtained PCR product to make circular DNA as pTJ002. The PCR conditions are as follows.
Primers
(SEQ ID NO. 21)
GB-140: GAGGAAATGGTCACAGGGCGAGAATAGGTTG
(SEQ ID NO. 22)
GB-141: GCCCTGTGACCATTTCCTCATTGTGCTGG

Reaction Solution Composition
Sterilized water 22 μl
2× PrimeSTAR (manufactured by Takara Bio) 25 μl
GB-140 (SEQ ID NO. 21) 1 μl
GB-141 (SEQ ID NO. 22) 1 μl
pTJ001 1 μl
Total amount 50 μl
Temperature Cycle
30 cycles of reaction at 98° C. 10 seconds, 50° C. 10 seconds and 72° C. 180 seconds
After PCR completion, upon performing confirmation of the fragment by 0.7% agarose gel electrophoresis using 1 μl of sample, amplification of the fragment was recognized. In the above-mentioned plasmid pTJ002 production procedure, a Wizard Genomic DNA Purification Kit (manufactured by Promega) was used in the genome extraction from PR4 strain, a Gel/PCR Purification Kit (manufactured by FAVORGEN) was used in the purification of DNA fragment digested with the restriction enzyme and the PCR product, a DNA Ligation Kit <Mighty Mix> (manufactured by Takara Bio) was used in the joining of DNA, and a QIAprep miniprep kit (manufactured by QIAGEN) was used in the extraction of plasmid.
Reference Example 4: Preparation of LigD Homolog Gene Deficient Derivative Strain of PR4KS
With the product by transforming E. coli (Escherichia coli) S17-1λpir by way of pTJ002 as the donor, and the PR4KS obtained by the method of Reference Example 2 as the recipient, conjugal transfer was performed similarly to the method described in Japanese Unexamined Patent Application, Publication No. 2011-200133 to obtain 13 strains of the LigD homolog gene deficient derivative strain produced by homologous recombination. One strain was selected from the deficient derivative strains, and named PR4KSΔligD.
Reference Example 5: Preparation of Plasmid pLK005 for Rhodococcus Bacterium and Nitrile Hydratase Expression Plasmid pSJ201 Using this
(1) Acquisition and Analysis of pLK005
Using pK4 (refer to Japanese Unexamined Patent Application, Publication No. H5-64589), Rhodococcus sp N775 (National Institute of Advanced Industrial Science and Technology, Patent Organism Depository, deposit number FERM BP-961) was transformed by the above-mentioned electroporation method. The obtained transformant was inoculated to 10 ml of MYK culture medium, and cultured at 30° C. for 1 day. Variation treatment was performed by exposing this to ultraviolet light inside a clean bench. The culture liquid in which variation treatment was performed was applied to MYK nutrient agar containing 50 to 400 μg/ml kanamycin, and cultured at 30° C. for 3 days.
The plurality of colonies appearing on the nutrient agar was respectively cultured in MYK culture medium, and plasmids were recovered from the transformants. Using the recovered plasmid, Rhodococcus sp N775 was transformed again, and it was investigated whether the kanamycin resistance of the transformant improves. As a result thereof, a number of strains of transformant for which the kanamycin resistance clearly improved were recognized.
Upon investigating the nucleotide sequences of plasmids for which kanamycin resistance was recognized as improving, it was recognized that a change occurs in the sequence in the upstream region of the kanamycin-resistant gene of pK4 (overlap of 8-nucleotide sequence GTTGTAGG). This plasmid for which this kanamycin resistance was recognized as improving was named pLK005.
(2) Preparation of pSJ040
The plasmid pSJ034 is a plasmid prepared from the plasmid pSJ023 by the method described in Japanese Unexamined Patent Application, Publication No. H10-337185. In pSJ034, although three EcoRI restriction enzymes sites are present, the plasmid pSJ040 was prepared in which one of these was transformed to a SpeI site. Specifically, pSJ034 was partially decomposed using restriction enzyme EcoRI. The cleavaged site was converted into blunt end using Takara Blunting kit and then ligation reaction was performed under the presence of SpeI linker. E. coli JM109 strain was transformed using the reaction solution. After culturing the transformant, plasmid was extracted, and the plasmid to which SpeI linker had been inserted was separated. Plasmid in which SpeI linker was inserted at, among the three EcoRI sites of pSJ034, the EcoRI site present downstream of the kanamycin-resistant gene was named pSJ040.
(3) Assembly of pSJ201
pLK005 was digested with HindIII to prepare a fragment of about 2.1 kb. On the other hand, pSJ040 was digested with HindIII to prepare a fragment of about 9.8 kb. Using these two fragments, the ligation reaction was performed, and E. coli JM109 strain was transformed using the reaction solution. After culturing the transformant, the plasmid was extracted and the nucleotide sequence thereof was confirmed, a result of which a plasmid keeping the mutated sequence (duplication of GTTGTAGG) derived from pLK005, and otherwise having the same sequence as pSJ040 was named pSJ201.
Reference Example 6: Preparation of RE_Acd1/RE_echA/RE_hchA/RE_mmsB Gene Deficient Derivative Strain of PR4KSΔligD Derivative Strain
(1) Preparation of Plasmid for Gene Deficiency Using in Fusion Method
The preparation of a plasmid for gene deficiency was performed by way of an In-Fusion HD Cloning kit (manufactured by Takara Bio) in which the RE_acd1/RE_echA/RE_hchA/RE_mmsB gene of PR4KS strain was the target gene (refer to FIG. 4).
The DNA of the upstream and downstream sequences of the target gene was amplified by PCR. The PCR conditions were as follows.
Primers for Fragment 1
(SEQ ID NO. 23)
MMA-061: CGACTCTAGAGGATCGCTCAGTACATCTACGAGAC
(SEQ ID NO. 24)
MMA-062: AGTGTGAGGAAAGTGTTCCGATCAGTTCAT

Primers for Fragment 2
(SEQ ID NO. 25)
MMA-063: CACTTTCCTCACACTCGTCGAGAGTATGAG
(SEQ ID NO. 26)
MMA-064: CGGTACCCGGGGATCAGCGCGACGAACAACGAGAC

Reaction Solution Composition
Template (PR4 wild type genomic DNA) 1 μL
2× PrimeSTAR Max Premix (manufactured by Takara Bio) 25 μL
Fw primer (20 μM) 1 μL
Rv primer (20 μM) 1 μL
D. W. 22 μL
Total amount 50 μl
Temperature Cycle
30 cycles of reaction at 98° C. 10 seconds, 60° C. 10 seconds and 72° C. 120 seconds
After PCR completion, upon performing confirmation of the fragment by 0.7% agarose gel electrophoresis using 1 μl of sample, amplification of the fragment was recognized. Using a Gel/PCR Purification Kit (manufactured by FAVORGEN), buffer substitution was performed on the PCR product (fragment 1 and fragment 2), and used in the reaction by the In-Fusion HD Cloning Kit shown below.
(2) Linkage of Target Fragment with Vector by in-Fusion HD Cloning Kit and Transformation
The linkage of the above-mentioned fragment and vector was performed using the In-Fusion HD Cloning Kit. The reaction conditions were as follows.
Reaction Solution Composition
5× In-Fusion HD Enzyme Premix 2 μL
Vector fragment 1.5 μL
DNA fragment 1 1 μL
DNA fragment 2 2 μL
D. W. 3.5 μL
Total amount 10 μL
After incubating the above-mentioned reaction solution at 50° C. for 15 minutes, it was cooled on ice, and used in the transformation of E. coli JM109 strain. The selection of E. coli transformant was performed with LB nutrient agar containing 50 mg/L kanamycin sulfate (hereinafter, LB Km 50 nutrient agar). Plasmid was prepared from the obtained transformant using a Mini prep Kit (QIAGEN) to obtain the target plasmid. Confirmation of the plasmid was performed by investigating the fragment size after XbaI restriction enzyme treatment, and the sequence of the linkage region of the insert fragment and vector. The target plasmid was named pMMA302.
(3) Preparation of Homologous Recombinant Derivative Strain of PR4KSΔligD Derivative Strain and Gene Deficient Derivative Strain
To 20 μl of PR4KSΔligD strain competent cell, 1 μl of pMMA302 was added, and incubated on ice for 10 minutes. The entire amount of the above-mentioned incubated solution was moved to an ice-cooled electroporation cuvet (0.1 cm), high voltage of 1.5 kV (200Ω) was applied, 600 μl of LB liquid culture medium was immediately added, and left to stand at 30° C. for 6 hours. On the LB nutrient agar containing 10 mg/L kanamycin sulfate (hereinafter, LB Km10 nutrient agar), 200 μl was spread and cultured at 30° C. for 4 days. The grown colony was streaked on the LB Km10 nutrient agar, and after culturing for 4 days, colony PCR was performed according to the conditions shown below and confirmation of the homologous recombinant derivative strain was performed.
Primers
(SEQ ID NO. 27)
MMA-069: GCGCATCTACAAGGAAGAGATC
(SEQ ID NO. 28)
MMA-070: GCGACGCTCATCGAGATCTC

Reaction Solution Composition
Template 4.0 μl
2× Mighty Amp Buffer (manufactured by Takara) 5.0 μl
Fw Primer (20 μm) 0.25 μl
Rv Primer (20 μm) 0.25 μl
D. W. 0.3 μl
Mighty Amp DNA Polymerase (manufactured by Takara) 0.2 μl
Total 10.0 μl
Temperature Cycle
30 cycles of reaction at 98° C. 10 seconds, and 68° C. 180 seconds
The colony recognized as being a homologous recombinant derivative strain was suspended in 200 μl of LB culture medium, 100 μl was spreadon LB+10% sucrose nutrient agar, and cultured for 3 days. From the grown colonies, those that came to be kanamycin sensitive were selected, and the target gene deficiency was confirmed for these by colony PCR. As a result thereof, a strain in which the four genes of RE_acd1, RE_echA, RE_hchA and RE_mmsB had been deleted from the PR4KSΔligD derivative strain was obtained, and named DMA008 strain.
Example 18: Preparation of Plasmid for ACD and AAT Co-Expression in Microorganism Belonging to Rhodococcus Genus
Plasmid for expressing ACD and/or AAT in microorganisms belonging to Rhodococcus genus was prepared.
A “nitrilase promoter+MpAAT1 gene” fragment obtained by PCR reaction with plasmid pAAT301 for MpAAT1 gene expression as the template was inserted downstream of the RE_acd1 gene of plasmid pMMA401 for RE_acd1 gene expression.
Amplification of the “nitrilase promoter+MpAAT1 gene” fragment was performed as follows.
Primers
MMA-133(Sse-ProFw):
(SEQ ID NO. 29)
TGACCTGCAGGTGCACTCCGCTGCGACATGTATCGA
MMA-131(Sse-001Rv):
(SEQ ID NO. 30)
ACTCTAGCCTGCAGGTCATTGACTAGTTGATCTAAGGTTGTTACA

PCR Reaction Composition
Template (pAAT301) 1 μl
2× PrimeSTAR Max Premix (manufactured by Takara) 10 μl
Fw Primer (10 μM) 0.6 μl
Rv Primer (10 μM) 0.6 μl
D. W. 7.8 μl
Total 20 μl
Temperature Cycle
30 cycles of reaction at 98° C. 5 seconds, 60° C. 5 seconds and 72° C. 45 seconds
The “nitrilase promoter+MpAAT1 gene” fragment obtained in this way was treated with restriction enzyme Sse8387I. On the other hand, after treatment with Sse8387I, SAP treatment was performed also on pMMA401. These DNA fragments were purified using a Gel/PCR Purification Kit (manufactured by FAVORGEN) after performing 0.7% agarose gel electrophoresis. The restriction enzyme treatment reaction conditions and ligation reaction conditions were as follows.
Restriction Enzyme Treatment Reaction Composition (AAT Fragment)
PCR amplified fragment 40 μl
10×M buffer 5 μl
0.1% BSA 4 μl
Sse8387I (manufactured by Takara) 1 μl
Total 50 μl
Restriction Enzyme Treatment Reaction Composition (Vector Fragment)
pMMA401 (vector) 3 μl
10×M buffer 4 μl
0.1% BSA 4 μl
AP 1 μl
Sse8387I (manufactured by Promega) 1 μl
D. W. 27 μl
Total 40 μl
Ligation Reaction Composition
pMMA401 1 μl
Insert fragment 2 μl
Ligation Mix (manufactured by Takara) 3 μl
Total 6 μl
Transformation of E. coli JM109 strain was performed using a ligation reaction solution mixed in the above-mentioned composition. Plasmid was extracted from the obtained transformant. After restriction enzyme Sse8387I treatment, agarose electrophoresis was performed, and it was confirmed that a fragment of the target size is being inserted. It was confirmed as being the target plasmid from the nucleotide sequence analysis of the linkage region of the insert fragment of the obtained plasmid, and the present plasmid was named pACDAAT1.
A total of six plasmids for ACD and AAT co-expression of different sequences (pACDAAT2, pACDAAT3, pACDAAT4, pACDAAT6 and pACDAAT8) were prepared using the same technique as the above-mentioned technique (refer to FIG. 5).
Example 19: Production of Butyl Methacrylate from ACD and AAT Co-Expressing Recombinant
DMA008 strain obtained in (3) of Reference Example 6 was transformed by plasmids pACDAAT1, pACDAAT2, pACDAAT3, pACDAAT4, pACDAAT6 and pACDAAT8, respectively. Using the obtained recombinants (DMA008/pACDAAT1, DMA008/pACDAAT2, DMA008/pACDAAT3, DMA008/pACDAAT4, DMA008/pACDAAT6 and DMA008/pACDAAT8), the production of methacrylic acid ester was performed by the resting microorganism reaction. In addition, DMA008/pLK005 was used as a control.
To 2 ml of LB Km 10 liquid culture medium (Wassermann test tube), 1 inoculating loop was inoculated, and was cultured for 2 days at 30° C. with a rotary shaker (180 rpm) under aerobic conditions (preculture). To 100 mL of LB Km 10 (culture medium 100 mL/500 mL three-neck flask), 1 ml of prebroth was inoculated, and culturing was performed for 3 days at 30° C. in a rotary shaker (230 rpm) under aerobic conditions (main culture).
After main culturing, 40 mL of the main broth was transferred to a 50 mL conical tube, and centrifuged (12,000 rpm, 10 min), to obtain the bacterial cell. Using this bacterial cell, the below reaction was performed. To a 10-ml glass sample bottle, 1 ml of reaction solution was added to carry out reaction for 18 hours at 30° C. in a rotary shaker (180 rpm) under aerobic conditions.
Reaction Solution Composition
OD630=10 bacterial cell (final concentration)
5.0 g/l 2-oxoisovaleric acid (final concentration)
40 mM alcohol (final concentration)
50 mM sodium phosphate buffer/pH 7.5 (final concentration)
n-butanol was used as the alcohol.
After reaction, 1 mL of acetonitrile was added to the reaction solution and well mixed, followed by filtering using a syringe filter DISMIC/pore size 0.45 μm (manufactured by ADVANTEC), and then analyzed with the HPLC analysis described in Example 9B. The analysis results of the product after 18 hours are shown in Table 10.
Formation of Butyl Methacrylate from ACD and AAT Co-Expressing Recombinant
TABLE 10
Recombinant Generated amount of butyl methacrylate (μM)
DMA008/pLK005 0
DMA008/pACDAAT1 7.51
DMA008/pACDAAT2 2.06
DMA008/pACDAAT3 4.34
DMA008/pACDAAT4 0.46
DMA008/pACDAAT6 2.18
DMA008/pACDAAT8 0.52
Example 20: Production of Methacrylic Acid Ester from ACD and AAT Co-Expressing Recombinant
The DMA008 strain obtained in (3) of Reference Example 6 was transformed by plasmid pACDAAT1, respectively. Using the obtained recombinant (DMA008/pACDAAT1), the production of methacrylic acid ester was performed by the resting microorganism reaction. In addition, DMA008/pLK005 was used as a control. Using the method described in Example 19, culturing of recombinant was carried out to obtain the bacterial cell.
Reaction Solution Composition
OD630=10 bacterial cell (final concentration)
5.0 g/l 2-oxoisovaleric acid (final concentration)
40 mM alcohol (final concentration)
50 mM sodium phosphate buffer/pH 7.5 (final concentration)
n-butanol, isobutanol and 2-ethylhexyl alcohol were used as the alcohol.
After reaction, 1 mL of acetonitrile was added to the reaction solution and well mixed, followed by filtering using a syringe filter DISMIC/pore size 0.45 μm (manufactured by ADVANTEC), and then analyzed with the HPLC analysis described in Example 9B. The analysis results of the product after 18 hours are shown in Table 11.
Formation of Methacrylic Acid Ester from ACD and AAT Co-Expressing Recombinant
TABLE 11
Generated amount (mM)
Isobutyl 2-ethylhexyl
Recombinant Butyl methacrylate methacrylate methacrylate
DMA008/pLK005 0 0 0
DMA008/pACDAAT1 0.01 0.006 0.02
Comparative Example 1 Synthesis Reaction of Methacrylic Acid Ester from Yeast-Derived AAT Gene Recombinant Cell-Free Extract
Yeast-derived AAT gene expressing plasmids were prepared similarly to Example 6 (Table 12), and E. coli was transformed using these to obtain AAT expressing recombinant.
Yeast-Derived AAT Gene Expression Plasmid
TABLE 12
Expression plasmid
SEQ ID NO Gene name Template plasmid pTrc99A pET16b
34 ATF1 pAAT005 pAAT105 pAAT205
36 ATF2 pAAT006 pAAT106 pAAT206
Cell-free extract was prepared similarly to Example 7, and the synthesis reaction of butyl methacrylate was performed with methacrylyl-CoA and n-butanol as substrate similarly to Example 8. As a result thereof, the formation of butyl methacrylate was not recognized. On the other hand, in the case of establishing acetyl-CoA and n-butanol as substrate, the formation of butyl acetate was recognized.
Formation of Ester Using Yeast-Derived AAT Gene Recombinant
TABLE 13
Generated amount (mM)
Butyl methacrylate Butyl acetate
Recombinant 1 hour 3 hours 5 hours 30 min 1 hour 3 hours
JM109/pAAT105 0 0 0 0.089 0.145 0.170
JM109/pAAT106 0 0 0 0.104 0.189 0.290
JM109/pTrc99A 0 0 0 0 0 0
SEQ ID NO. 11: MMA-044
SEQ ID NO. 12: MMA-045
SEQ ID NO. 13: MMA-003
SEQ ID NO. 14: MMA-004
SEQ ID NO. 15: MMA-031
SEQ ID NO. 16: MMA-032
SEQ ID NO. 17: MAA-15
SEQ ID NO. 18: MAA-16
SEQ ID NO. 19: GB-138
SEQ ID NO. 20: GB-139
SEQ ID NO. 21: GB-140
SEQ ID NO. 22: GB-141
SEQ ID NO. 23: MMA-061
SEQ ID NO. 24: MMA-062
SEQ ID NO. 25: MMA-063
SEQ ID NO. 26: MMA-064
SEQ ID NO. 27: MMA-069
SEQ ID NO. 28: MMA-070
SEQ ID NO. 29: MMA-133
SEQ ID NO. 30: MMA-131

Claims (10)

The invention claimed is:
1. A method for producing methacrylic acid ester, the method comprising:
transforming isobutyryl-CoA or 3-hydroxyisobutyryl-CoA to form methacrylyl-CoA, and
contacting methacrylyl-CoA with an alcohol or a phenol in the presence of an alcohol acyltransferase, wherein the methacrylic acid ester accumulated has a concentration of at least 0.001 mM, and wherein the alcohol acyltransferase is of plant origin and wherein the plant belongs to a genus of Malus.
2. The method for producing a methacrylic acid ester according to claim 1, comprising transforming isobutyryl-CoA to form the methacrylyl-CoA, wherein the isobutyryl-CoA is produced from 2-oxoisovaleric acid.
3. The method for producing a methacrylic acid ester according to claim 1, wherein said alcohol or phenol is a linear or branched C1-10 unsubstituted alcohol, aralkyl alcohol or phenol.
4. The method for producing a methacrylic acid ester according to claim 3, wherein the methacrylic acid ester accumulated has a concentration of at least 0.010 mM.
5. The method for producing a methacrylic acid ester according to claim 1, wherein the methacrylic acid ester accumulated has a concentration of at least 0.010 mM.
6. The method for producing a methacrylic acid ester according to claim 1, wherein said alcohol or phenol is selected from the group consisting of methanol, ethanol, n-propanol, isopropanol, n-butanol, isobutanol, sec-butanol, tert-butanol, n-pentylalcohol, isopentyl alcohol, tert-pentyl alcohol, n-hexyl alcohol, isohexyl alcohol, 2-hexyl alcohol, dimethylbutyl alcohol, ethylbutyl alcohol, heptyl alcohol, octyl alcohol, 2-ethylhexyl alcohol, benzyl alcohol and phenol.
7. The method for producing a methacrylic acid ester according to claim 1, wherein the methacrylic acid ester accumulated has a concentration of at least 0.010 mM.
8. The method for producing methacrylic acid ester according to claim 1, wherein the alcohol acyltransferase is expressed by a genetically modified microorganism that has been transformed to express the alcohol acyltransferase.
9. The method for producing methacrylic acid ester according to claim 8, wherein the genetically modified microorganism belongs to the Rhodococcus genus.
10. A method for producing a methacrylic acid ester, the method comprising:
transforming isobutyryl-CoA or 3-hydroxyisobutyryl-CoA to form methacrylyl-CoA, and
contacting methacrylyl-CoA with an alcohol or a phenol in the presence of an alcohol acyltransferase, wherein the methacrylic acid ester accumulated has a concentration of at least 0.001 mM, and wherein the alcohol acyltransferase is of plant origin and wherein said plant is selected from the group consisting of Malus pumila, Malus domestica, Malus baccata, Malus halliana, Malus floribunda, and Malus prunifolia.
US14/405,593 2012-09-10 2013-09-10 Method for producing methacrylic acid ester Active US10851392B2 (en)

Applications Claiming Priority (7)

Application Number Priority Date Filing Date Title
JP2012-198840 2012-09-10
JP2012198840 2012-09-10
JP2013-160300 2013-08-01
JP2013160300 2013-08-01
JP2013170404 2013-08-20
JP2013-170404 2013-08-20
PCT/JP2013/005354 WO2014038214A1 (en) 2012-09-10 2013-09-10 Method for producing methacrylic acid ester

Publications (2)

Publication Number Publication Date
US20150184207A1 US20150184207A1 (en) 2015-07-02
US10851392B2 true US10851392B2 (en) 2020-12-01

Family

ID=50236843

Family Applications (1)

Application Number Title Priority Date Filing Date
US14/405,593 Active US10851392B2 (en) 2012-09-10 2013-09-10 Method for producing methacrylic acid ester

Country Status (10)

Country Link
US (1) US10851392B2 (en)
EP (2) EP2848694B1 (en)
JP (2) JP6146308B2 (en)
KR (1) KR101561793B1 (en)
CN (1) CN104619851B (en)
AU (2) AU2016202343A1 (en)
BR (1) BR112015000069B1 (en)
DK (1) DK2848694T3 (en)
ES (1) ES2689477T3 (en)
WO (1) WO2014038214A1 (en)

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2848694B1 (en) 2012-09-10 2018-08-01 Mitsubishi Chemical Corporation Method for producing methacrylic acid ester
JP6202001B2 (en) * 2013-08-01 2017-09-27 三菱ケミカル株式会社 Method for producing methacrylyl-CoA
KR20160108546A (en) * 2014-03-07 2016-09-19 미쯔비시 레이온 가부시끼가이샤 Method for producing methacrylic acid ester, and novel methacrylic acid ester synthase
CN104830726B (en) * 2015-05-06 2018-04-03 重庆理工大学 Degradating chloro hydrocarbon composite bacteria agent and its application
MY198780A (en) * 2015-05-19 2023-09-27 Mitsubishi Chemical Uk Ltd Process for the biological production of methacrylic acid and derivatives thereof
WO2017069267A1 (en) * 2015-10-23 2017-04-27 ザ リージェンツ オブ ザ ユニバーシティ オブ カリフォルニア Biological production of methyl methacrylate
US11913054B2 (en) * 2016-03-30 2024-02-27 Basf Se Fermentative production of n-butylacrylate using alcohol acyl transferase enzymes
WO2018043546A1 (en) 2016-08-30 2018-03-08 三菱ケミカル株式会社 Method for producing mutant enzyme, and mutant alcohol acyltransferase
GB201619827D0 (en) * 2016-11-23 2017-01-04 Lucite Int Uk Ltd Process for the production of methyl methacrylate
BR112020016295A2 (en) * 2018-03-02 2020-12-15 Mitsubishi Chemical Corporation METHOD FOR THE PRODUCTION OF 3-HYDROXY-ISOBUTYRIC ACID ESTER AND METHACRYLIC ESTER
MY195514A (en) * 2018-08-09 2023-01-29 Hartalega Res Sdn Bhd Chitosan Coated Calcium Alginate Bacteria Beads for Ammonia Removal in Wastewater Treatment With Bioaugmentation
CN110079475B (en) * 2019-04-15 2021-04-23 广西大学 Method for degrading agar by utilizing microbial fermentation of various antibiotics for inhibiting mixed bacteria
CN110025629B (en) * 2019-05-23 2021-03-26 河南大学 Application of filamental flowering crab polysaccharide in preparing immunity enhancing medicine
GB2621337A (en) 2022-08-08 2024-02-14 Mitsubishi Chemical Uk Ltd Process for the biological production of methacrylic acid and derivatives thereof

Citations (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5446887A (en) 1977-09-19 1979-04-13 Nitto Chem Ind Co Ltd Preparation of acrylic acid or methacrylic acid
EP0187680A2 (en) 1985-01-11 1986-07-16 Nitto Kagaku Kogyo Kabushiki Kaisha Process for producing organic acids by use of microorganisms
JPS6214788A (en) 1985-07-12 1987-01-23 Res Assoc Util Of Light Oil Production of methacrylic acid
JPH01132392A (en) 1987-11-18 1989-05-24 Res Assoc Util Of Light Oil Microbiological production of monocarboxylic acid
JPH0564589A (en) 1991-03-04 1993-03-19 Teruhiko Beppu Composite plasmid vector and transformed microorganism
JPH10248578A (en) 1997-03-05 1998-09-22 Nitto Chem Ind Co Ltd Expression vector for bacterium of genus rhodococcus
JPH10337185A (en) 1997-06-06 1998-12-22 Mitsubishi Rayon Co Ltd New protein having aspartase activity and genetic dna encoding the same
WO2000032789A1 (en) 1998-12-02 2000-06-08 Centrum Voor Plantenveredelings- En Reproduktieonderzoek (Cpro-Dlo) Fruit flavour related genes and use thereof
US20030148480A1 (en) 2002-02-05 2003-08-07 Dicosimo Robert Method for producing methacrylic acid acrylic acid with a combination of enzyme catalysts
JP2004514431A (en) 2000-11-20 2004-05-20 カーギル　インコーポレイテッド 3-hydroxypropionic acid and other organic compounds
WO2005090586A1 (en) 2004-03-19 2005-09-29 Ciba Specialty Chemicals Water Treatments Limited Biocatalytic manufacturing of (meth)acrylylcholine or 2-(n,n-dimethylamino)ethyl (meth)acrylate
WO2007039415A1 (en) 2005-09-19 2007-04-12 Ciba Specialty Chemicals Holding Inc. Biocatalytic manufacturing of (meth)acrylic esters
WO2007110394A2 (en) 2006-03-24 2007-10-04 Evonik Röhm Gmbh Method for the enzymatic production of 2-hydroxy-2-methyl carboxylic acids
WO2008145737A1 (en) 2007-06-01 2008-12-04 Evonik Degussa Gmbh A process for preparing methacrylic acid or methacrylic esters
US20090275096A1 (en) 2008-05-01 2009-11-05 Genomatica, Inc. Microorganisms for the production of methacrylic acid
US20100291644A1 (en) 2006-06-02 2010-11-18 Evonik Roehm Gmbh Process for preparing methacrylic acid or methacrylic esters
WO2011031897A1 (en) 2009-09-09 2011-03-17 Genomatica, Inc. Microorganisms and methods for the co-production of isopropanol with primary alcohols, diols and acids
JP2011200133A (en) 2010-03-24 2011-10-13 Mitsubishi Rayon Co Ltd Method for producing genetically modified microorganism
WO2012135789A2 (en) 2011-04-01 2012-10-04 Genomatica, Inc. Microorganisms for producing methacrylic acid and methacrylate esters and methods related thereto
JP2012198840A (en) 2011-03-23 2012-10-18 Hitachi Solutions Ltd Imaging management system and method for assisting model selection
JP2013160300A (en) 2012-02-06 2013-08-19 Kyb Co Ltd Caliper brake device
JP2013160302A (en) 2012-02-06 2013-08-19 Toyota Motor Corp Belt, element molding method, and molding device
WO2015015784A1 (en) 2013-08-01 2015-02-05 三菱レイヨン株式会社 METHOD FOR PRODUCING METHACRYLYL-CoA

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3355939B2 (en) 1996-07-10 2002-12-09 三菱自動車工業株式会社 Undercover for vehicle engine
JP2013170404A (en) 2012-02-21 2013-09-02 Jihei Kaneko Retaining wall block, retaining wall and construction method of retaining wall
EP2848694B1 (en) 2012-09-10 2018-08-01 Mitsubishi Chemical Corporation Method for producing methacrylic acid ester

Patent Citations (35)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5446887A (en) 1977-09-19 1979-04-13 Nitto Chem Ind Co Ltd Preparation of acrylic acid or methacrylic acid
EP0187680A2 (en) 1985-01-11 1986-07-16 Nitto Kagaku Kogyo Kabushiki Kaisha Process for producing organic acids by use of microorganisms
JPS61162191A (en) 1985-01-11 1986-07-22 Nitto Chem Ind Co Ltd Production of organic acid with bacterium
JPS6214788A (en) 1985-07-12 1987-01-23 Res Assoc Util Of Light Oil Production of methacrylic acid
JPH01132392A (en) 1987-11-18 1989-05-24 Res Assoc Util Of Light Oil Microbiological production of monocarboxylic acid
JPH0564589A (en) 1991-03-04 1993-03-19 Teruhiko Beppu Composite plasmid vector and transformed microorganism
JPH10248578A (en) 1997-03-05 1998-09-22 Nitto Chem Ind Co Ltd Expression vector for bacterium of genus rhodococcus
JPH10337185A (en) 1997-06-06 1998-12-22 Mitsubishi Rayon Co Ltd New protein having aspartase activity and genetic dna encoding the same
WO2000032789A1 (en) 1998-12-02 2000-06-08 Centrum Voor Plantenveredelings- En Reproduktieonderzoek (Cpro-Dlo) Fruit flavour related genes and use thereof
JP2004514431A (en) 2000-11-20 2004-05-20 カーギル　インコーポレイテッド 3-hydroxypropionic acid and other organic compounds
US20080076167A1 (en) 2000-11-20 2008-03-27 Cargill, Incorporated 3-hydroxypropionic acid and other organic compounds
JP2005516622A (en) 2002-02-05 2005-06-09 イー・アイ・デュポン・ドウ・ヌムール・アンド・カンパニー Method for producing methacrylic acid and acrylic acid using complex enzyme catalyst
US20030148480A1 (en) 2002-02-05 2003-08-07 Dicosimo Robert Method for producing methacrylic acid acrylic acid with a combination of enzyme catalysts
WO2005090586A1 (en) 2004-03-19 2005-09-29 Ciba Specialty Chemicals Water Treatments Limited Biocatalytic manufacturing of (meth)acrylylcholine or 2-(n,n-dimethylamino)ethyl (meth)acrylate
WO2007039415A1 (en) 2005-09-19 2007-04-12 Ciba Specialty Chemicals Holding Inc. Biocatalytic manufacturing of (meth)acrylic esters
US20090130729A1 (en) 2005-09-19 2009-05-21 Kenneth Charles Symes Biocatalytic manufacturing of (meth) acrylic esters
WO2007110394A2 (en) 2006-03-24 2007-10-04 Evonik Röhm Gmbh Method for the enzymatic production of 2-hydroxy-2-methyl carboxylic acids
US20110165640A1 (en) 2006-03-24 2011-07-07 Evonik Roehm Gmbh Method for the enzymatic production of 2-hydroxy-2-methyl carboxylic acids
JP2009538118A (en) 2006-03-24 2009-11-05 エボニック レーム ゲゼルシャフト ミット ベシュレンクテル ハフツング Enzymatic production of 2-hydroxy-2-methylcarboxylic acid
US20100291644A1 (en) 2006-06-02 2010-11-18 Evonik Roehm Gmbh Process for preparing methacrylic acid or methacrylic esters
WO2008145737A1 (en) 2007-06-01 2008-12-04 Evonik Degussa Gmbh A process for preparing methacrylic acid or methacrylic esters
JP2010528597A (en) 2007-06-01 2010-08-26 エボニック レーム ゲゼルシャフト ミット ベシュレンクテル ハフツング Method for producing methacrylic acid or methacrylic ester
CA2688292A1 (en) 2007-06-01 2008-12-04 Evonik Roehm Gmbh A process for preparing methacrylic acid or methacrylic esters
WO2009135074A2 (en) 2008-05-01 2009-11-05 Genomatica, Inc. Microorganisms for the production of methacrylic acid
US20090275096A1 (en) 2008-05-01 2009-11-05 Genomatica, Inc. Microorganisms for the production of methacrylic acid
JP2011519561A (en) 2008-05-01 2011-07-14 ジェノマティカ， インコーポレイテッド Microorganisms for the production of methacrylic acid
WO2011031897A1 (en) 2009-09-09 2011-03-17 Genomatica, Inc. Microorganisms and methods for the co-production of isopropanol with primary alcohols, diols and acids
JP2011200133A (en) 2010-03-24 2011-10-13 Mitsubishi Rayon Co Ltd Method for producing genetically modified microorganism
JP2012198840A (en) 2011-03-23 2012-10-18 Hitachi Solutions Ltd Imaging management system and method for assisting model selection
WO2012135789A2 (en) 2011-04-01 2012-10-04 Genomatica, Inc. Microorganisms for producing methacrylic acid and methacrylate esters and methods related thereto
US20130065279A1 (en) 2011-04-01 2013-03-14 Genomatica, Inc. Microorganisms for producing methacrylic acid and methacrylate esters and methods related thereto
JP2013160300A (en) 2012-02-06 2013-08-19 Kyb Co Ltd Caliper brake device
JP2013160302A (en) 2012-02-06 2013-08-19 Toyota Motor Corp Belt, element molding method, and molding device
WO2015015784A1 (en) 2013-08-01 2015-02-05 三菱レイヨン株式会社 METHOD FOR PRODUCING METHACRYLYL-CoA
EP3029145A1 (en) 2013-08-01 2016-06-08 Mitsubishi Rayon Co., Ltd. METHOD FOR PRODUCING METHACRYLYL-CoA

Non-Patent Citations (36)

* Cited by examiner, † Cited by third party
Title
"Making Esters" Extract from Chemguide, https://www.chemguide.co.uk/organicprops/esters/preparation.html, 2004, pp. 1-5.
Aharoni, A., "Identification of the SAAT Gene Involved in Strawberry Flavor Biogenesis by Use of DNA Microarrays", The Plant Cell, vol. 12, May 2000, pp. 647-661.
Baltoni'n et al., "VpAAT1, a Gene Encoding an Alcohol Acyltransferase, Is Involved in Ester Biosynthesis during Ripening of Mountain Papaya Fruit", J. Agric. Food Chem. 2010, 58, 5114-5121. DOI:10.1021/jf904296c. *
Beekwilder et al., "Functional Characterization of Enzymes Forming Volatile Esters from Strawberry and Banana", Plant Physiology, Aug. 2004, vol. 135, pp. 1865-1878. *
Birgitta Bremer, et al., "An update of the Angiosperm Phylogeny Group classification for the orders and families of flowering plants APG III" Botanical Journal of the Linnean Society, vol. 161, 2009, pp. 105-121.
Catherine Emily Horton, et al., "Ester production in E. coli and C. acetobutylicum" Enzyme and Microbial Technology, vol. 38, No. 7, XP027948848, 2006, pp. 937-943.
D'AURIA, J.C.: "Acyltransferases in plants: a good time to be BAHD", CURRENT OPINION IN PLANT BIOLOGY, ELSEVIER, AMSTERDAM, NL, vol. 9, no. 3, 1 June 2006 (2006-06-01), AMSTERDAM, NL, pages 331 - 340, XP028014883, ISSN: 1369-5266, DOI: 10.1016/j.pbi.2006.03.016
EDWIGE J. F. SOULEYRE, DAVID R. GREENWOOD, ELLEN N. FRIEL, SAKUNTALA KARUNAIRETNAM, RICHARD D. NEWCOMB: "An alcohol acyl transferase from apple (cv. Royal Gala), MpAAT1, produces esters involved in apple fruit flavor", FEBS JOURNAL, PUBLISHED BY BLACKWELL PUB. ON BEHALF OF THE FEDERATION OF EUROPEAN BIOCHEMICAL SOCIETIES, vol. 272, no. 12, 14 June 2005 (2005-06-14), pages 3132 - 3144, XP055197639, ISSN: 1742464X, DOI: 10.1111/j.1742-4658.2005.04732.x
Edwige J. F. Souleyre, et al., "An alcohol acyl transferase from apple (cv. Royal Gala), MpAAT1, produces esters involved in apple fruit flavor" FEBS Journal, vol. 272, No. 12, XP055197639, 2005, pp. 3132-3144.
European Office Action dated Mar. 23, 2020 in Patent Application No. 18175984.6, 10 pages.
Extended European Search Report dated Jul. 6, 2015 in Patent Application No. 13834617.6.
Extended European Search Report dated Oct. 8, 2018 in Patent Application No. 18175984.6.
G. Ozcan, et al., "Effect of Enzymes on Strawberry Volatiles during Storage, at Different Ripeness Level, in Different Cultivars, and during Eating", Journal of Food Science, vol. 75, No. 2, 2011, pp. C324-C333.
HORTON, C.E. ; BENNETT, G.N.: "Ester production in E. coli and C. acetobutylicum", ENZYME AND MICROBIAL TECHNOLOGY, STONEHAM, MA, US, vol. 38, no. 7, 2 May 2006 (2006-05-02), US, pages 937 - 943, XP027948848, ISSN: 0141-0229
International Search Report dated Nov. 19, 2013 in PCT/JP2013/005354 filed Sep. 10, 2013.
John C. D'Auria, "Acyltransferases in plants: a good time to be BAHD" Current Opinion in Plant Biology, vol. 9, No. 3, XP028014883, 2006, pp. 331-340.
John W. Hawes, "[8] Synthesis of Methacrylyl-CoA and (R)- and (S)-3-Hydroxyisobutyryl-CoA" Methods in Enzymology, vol. 324, 2000, pp. 73-79.
Mark R. Smith, et al., "The Utilization of 3-Mercapto-2-Methylpropionate as Sulphur Source by a Phototrophic Bacterium" Bioorganic & Medicinal Chemistry, vol. 2, No. 7, 1994, pp. 589-593.
Natalia Korotkova, et al., "Glyoxylate Regeneration Pathway in the Methylotroph Methylobacterium extorquens AM1", Journal of Bacteriology, vol. 184, No. 6, Mar. 2002, pp. 1750-1758.
Notice of Opposition in European Application No. EP13834617.6, issued Apr. 26, 2019.
Office Action dated Aug. 27, 2018 in India Patent Application No. 595/CHENP/2015.
Office Action dated May 15, 2018 in Chinese Patent Application No. 201380047196.3 with English translation.
Office Action dated Oct. 11, 2018 in European Patent Application No. 13 835 104.4.
Office Action in corresponding Chinese Application No. 2013800471963 dated Jul. 20, 2020. (w/English Translation).
Office Action in corresponding European Application No. 18175984.6, dated Jun. 10, 2020.
Ozcan, G., "Effect of Enzymes of Strawberry Volatiles During Storage, at Different Ripeness Level, in Different Cultivars and During Eating", 2010, The Ohio State University.
Quintana et al., "Molecular docking simulation analysis of alcohol acyltransferases from two related fruit species explains their different substrate selectivities", Molecular Simulation, 38(11):912-921. *
Sang-Hyun Pyo, et al., "A new route for the synthesis of methacrylic acid from 2-methyl-1,3-propanediol by integrating biotransofmration and catalytic dehydration" Green Chemistry, vol. 14, 2012, pp. 1942-1948.
Sompoch Noichinda, et al. "Subcellular Localization of Alcohol Acetyltransferase in Strawberry Fruit" Food Sci. Technol., vol. 5, No. 3, 1999, pp. 239-242.
Souleyre et al., "An alcohol acyl transferase from apple (cv. Royal Gala), MpAAT1, produces esters involved in apple fruit flavor", FEBS Journal 272 (2005) 3132-3144. *
Summons to attend oral proceedings pursuant to Rule 115(1) EPC issued on Feb. 20, 2020 in European Patent Application No. 13834617.6, 12 pages.
Toru Nagasawa, et al., "Production of acrylic acid and methacrylic acid using Rhodococcus rhodochrous J1 nitrilase", Applied Microbiology and Biotechnology, vol. 34, 1990, pp. 322-324.
Wanders, R., "Enzymology of the Branched-Chain Amino Acid Oxidation Disorders: The Valine Pathway", J. Inherit Metab. Dis., vol. 35, 2012, pp. 5-12.
Wu, W., "Stereospecificity of the Reaction Catalyzed by Enoyl-CoA Hydratase", Journal of the American Chemical Society, vol. 122, No. 17, May 3, 2000, pp. 3987-3994.
Yamashita, I., "Formation of Volatile Esters in Strawberries", Agr. Biol. Chem., vol. 39, No. 12, 1975, pp. 2303-2307.
Ying-Xin Zhang, et al., "Genes encoding acyl-CoA dehydrogenase (AcdH) homologues from Streptomyces coelicolor and Streptomyces avermitilis provide insights into the metabolism of small branched-chain fatty acids and macrolide antibiotic production" Microbiology, vol. 145, 1999, pp. 2323-2334.

Also Published As

Publication number Publication date
EP2848694B1 (en) 2018-08-01
CN104619851B (en) 2019-03-19
BR112015000069A8 (en) 2018-01-02
ES2689477T3 (en) 2018-11-14
AU2013314151A1 (en) 2015-02-19
KR101561793B1 (en) 2015-10-19
EP3395951A2 (en) 2018-10-31
EP3395951A3 (en) 2018-11-07
JPWO2014038214A1 (en) 2016-08-08
KR20140091740A (en) 2014-07-22
EP2848694A1 (en) 2015-03-18
EP2848694A4 (en) 2015-08-05
AU2016202343A1 (en) 2016-05-05
US20150184207A1 (en) 2015-07-02
JP6146308B2 (en) 2017-06-14
WO2014038214A1 (en) 2014-03-13
AU2016203106A1 (en) 2016-06-02
DK2848694T3 (en) 2018-09-03
JP2017136076A (en) 2017-08-10
AU2016203106B2 (en) 2017-07-27
BR112015000069A2 (en) 2017-08-08
AU2013314151B2 (en) 2016-03-17
CN104619851A (en) 2015-05-13
BR112015000069B1 (en) 2022-06-21

Similar Documents

Publication Publication Date Title
AU2016203106B2 (en) Method for producing methacrylic acid ester
US10294500B2 (en) Method for producing methacrylic acid and/or ester thereof
JP2015116141A (en) Isobutyric acid ester-producing microorganisms and methods for producing isobutyric acid ester
CN107075464A (en) The recombinant microorganism of alkene is produced from acetyl-COA
US20220235385A1 (en) Engineered microorganisms and methods for improved aldehyde dehydrogenase activity
EP3877525A2 (en) Co-production pathway for 3-hp and acetyl-coa derivatives from malonate semialdehyde
US10676766B2 (en) Biological production of methyl methacrylate
CN116783281A (en) Methods and compositions for preparing amide compounds

Legal Events

Date Code Title Description
AS Assignment

Owner name: MITSUBISHI RAYON CO., LTD., JAPAN

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:SATO, EIJI;YU, FUJIO;MIZUNASHI, WATARU;AND OTHERS;SIGNING DATES FROM 20141015 TO 20141029;REEL/FRAME:034377/0897

AS Assignment

Owner name: MITSUBISHI CHEMICAL CORPORATION, JAPAN

Free format text: CHANGE OF NAME;ASSIGNOR:MITSUBISHI RAYON CO., LTD.;REEL/FRAME:043136/0132

Effective date: 20170403

STPP Information on status: patent application and granting procedure in general

Free format text: FINAL REJECTION MAILED

STCV Information on status: appeal procedure

Free format text: NOTICE OF APPEAL FILED

STCV Information on status: appeal procedure

Free format text: NOTICE OF APPEAL FILED

STPP Information on status: patent application and granting procedure in general

Free format text: DOCKETED NEW CASE - READY FOR EXAMINATION

STPP Information on status: patent application and granting procedure in general

Free format text: NON FINAL ACTION MAILED

STPP Information on status: patent application and granting procedure in general

Free format text: FINAL REJECTION MAILED

STCF Information on status: patent grant

Free format text: PATENTED CASE